EP2739708B1 - Verwendung von additiven in kraftstoffzusammensetzungen - Google Patents

Verwendung von additiven in kraftstoffzusammensetzungen Download PDF

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EP2739708B1
EP2739708B1 EP12756807.9A EP12756807A EP2739708B1 EP 2739708 B1 EP2739708 B1 EP 2739708B1 EP 12756807 A EP12756807 A EP 12756807A EP 2739708 B1 EP2739708 B1 EP 2739708B1
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fuel
additive
hydrocarbyl
component
substituted
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EP2739708A1 (de
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Jacqueline Reid
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Innospec Ltd
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Innospec Ltd
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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/146—Macromolecular compounds according to different macromolecular groups, mixtures thereof
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00—Use of additives to fuels or fires for particular purposes
    • C10L10/04—Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/22—Organic compounds containing nitrogen
    • C10L1/234—Macromolecular compounds
    • C10L1/238—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/22—Organic compounds containing nitrogen
    • C10L1/234—Macromolecular compounds
    • C10L1/238—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/2383—Polyamines or polyimines, or derivatives thereof (poly)amines and imines; derivatives thereof (substituted by a macromolecular group containing 30C)
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00—Use of additives to fuels or fires for particular purposes
    • C10L10/18—Use 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
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/16—Hydrocarbons
    • C10L1/1616—Hydrocarbons fractions, e.g. lubricants, solvents, naphta, bitumen, tars, terpentine
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/192—Macromolecular compounds
    • C10L1/198—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/192—Macromolecular compounds
    • C10L1/198—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
    • C10L1/1981—Condensation polymers of aldehydes or ketones
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/22—Organic compounds containing nitrogen
    • C10L1/234—Macromolecular compounds
    • C10L1/238—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/2383—Polyamines or polyimines, or derivatives thereof (poly)amines and imines; derivatives thereof (substituted by a macromolecular group containing 30C)
    • C10L1/2387—Polyoxyalkyleneamines (poly)oxyalkylene amines and derivatives thereof (substituted by a macromolecular group containing 30C)
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/28—Organic compounds containing silicon
    • C10L1/285—Organic compounds containing silicon macromolecular compounds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2230/00—Function and purpose of a components of a fuel or the composition as a whole
    • C10L2230/08—Inhibitors
    • C10L2230/086—Demulsifiers
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2270/00—Specifically adapted fuels
    • C10L2270/02—Specifically adapted fuels for internal combustion engines
    • C10L2270/026—Specifically adapted fuels for internal combustion engines for diesel engines, e.g. automobiles, stationary, marine
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2300/00—Mixture of two or more additives covered by the same group of C10L1/00 - C10L1/308
    • C10L2300/20—Mixture of two components

Definitions

  • the present invention relates to the use of additives for diesel fuel compositions, especially those suitable for use in modern diesel engines with high pressure fuel systems.
  • Diesel engines having high pressure fuel systems can include but are not limited to heavy duty diesel engines and smaller passenger car type diesel engines.
  • Heavy duty diesel engines can include very powerful engines such as the MTU series 4000 diesel having 20 cylinder variants designed primarily for ships and power generation with power output up to 4300 kW or engines such as the Renault dXi 7 having 6 cylinders and a power output around 240kW.
  • a typical passenger car diesel engine is the Ford DW10 having 4 cylinders and power output of 100 kW or less depending on the variant.
  • a common feature is a high pressure fuel system. Typically pressures in excess of 1350 bar (1.35 x 10 8 Pa) are used but often pressures of up to 2000 bar (2 x 10 8 Pa) or more may exist.
  • high pressure fuel systems Two non-limiting examples of such high pressure fuel systems are: the common rail injection system, in which the fuel is compressed utilizing a high-pressure pump that supplies it to the fuel injection valves through a common rail; and the unit injection system which integrates the high-pressure pump and fuel injection valve in one assembly, achieving the highest possible injection pressures exceeding 2000 bar (2 x 10 8 Pa). In both systems, in pressurising the fuel, the fuel gets hot, often to temperatures around 100oC, or above.
  • the fuel is stored at high pressure in the central accumulator rail or separate accumulators prior to being delivered to the injectors. Often, some of the heated fuel is returned to the low pressure side of the fuel system or returned to the fuel tank. In unit injection systems the fuel is compressed within the injector in order to generate the high injection pressures. This in turn increases the temperature of the fuel.
  • fuel is present in the injector body prior to injection where it is heated further due to heat from the combustion chamber.
  • the temperature of the fuel at the tip of the injector can be as high as 250 - 350 oC.
  • a common problem with diesel engines is fouling of the injector, particularly the injector body, and the injector nozzle. Fouling may also occur in the fuel filter. Injector nozzle fouling occurs when the nozzle becomes blocked with deposits from the diesel fuel. Fouling of fuel filters may be related to the recirculation of fuel back to the fuel tank. Deposits increase with degradation of the fuel. Deposits may take the form of carbonaceous coke-like residues or sticky or gum-like residues. Diesel fuels become more and more unstable the more they are heated, particularly if heated under pressure. Thus diesel engines having high pressure fuel systems may cause increased fuel degradation.
  • injector fouling may occur when using any type of diesel fuels.
  • some fuels may be particularly prone to cause fouling or fouling may occur more quickly when these fuels are used.
  • fuels containing biodiesel have been found to produce injector fouling more readily.
  • Diesel fuels containing metallic species may also lead to increased deposits.
  • Metallic species may be deliberately added to a fuel in additive compositions or may be present as contaminant species. Contamination occurs if metallic species from fuel distribution systems, vehicle distribution systems, vehicle fuel systems, other metallic components and lubricating oils become dissolved or dispersed in fuel.
  • Transition metals in particular cause increased deposits, especially copper and zinc species. These may be typically present at levels from a few ppb (parts per billion) up to 50 ppm, but it is believed that levels likely to cause problems are from 0.1 to 50 ppm, for example 0.1 to 10 ppm.
  • US2010/263261 describes a diesel fuel composition comprising a performance enhancing additive which is the product of a Mannich reaction between: (a) an aldehyde; (b) a polyamine; and (c) an optionally substituted phenol; wherein the polyamine component (b) includes the moiety R 1 R 2 NCHR 3 CHR 4 NR 5 R 6 wherein each of R 1 , R 2 , R3, R 4 , R 5 and R 6 is independently selected from hydrogen, and an optionally substituted alkyl, alkenyl, alkynyl, aryl, alkylaryl or arylalkyl substituent.
  • WO2010/097624 decribes a method of removing deposits from a diesel engine by combusting in the engine a diesel fuel composition
  • a diesel fuel composition comprising an engine cleaning additive which is the product of a Mannich reaction between: (a) an aldehyde; (b) ammonia, hydrazine or an amine; and (c) an optionally substituted phenol; wherein the or each substituent of the phenol component (c) has an average molecular weight of less than 400.
  • WO2010/132259 relates to quaternary ammonium amide and/or ester salts and their use as additives, including their use in fuels, such as diesel fuel.
  • US2010/263262 describes an aviation gasoline formed by blending (i) an unleaded base fuel having a base MON of at least 94, with (ii) at least one aromatic amine effective to provide the base fuel with a final MON of at least 100.
  • nitrogen-containing detergents may be added to diesel fuel to reduce coking.
  • Typical nitrogen-containing detergents are those formed by the reaction of a polyisobutylene-substituted succinic acid derivative with a polyalkylene polyamine.
  • newer engines including finer injector nozzles are more sensitive and current diesel fuels may not be suitable for use with the new engines incorporating these smaller nozzle holes.
  • the present inventor has developed diesel fuel compositions which when used in diesel engines having high pressure fuel systems provide improved performance compared with diesel fuel compositions of the prior art.
  • Such fuel compositions may be considered to perform a "keep clean" function i.e. they prevent or inhibit fouling.
  • compositions reduce the fouling of vehicle fuel filters. It would be useful to provide compositions that prevent or inhibit the occurrence of fuel filter deposits i.e, provide a "keep clean” function. It would be useful to provide compositions that remove existing deposits from fuel filter deposits i.e. provide a "clean up” function. Compositions able to provide both of these functions would be especially useful.
  • a first additive (i) comprising a quaternary ammonium salt and a second additive (ii) comprising a Mannich reaction product in a diesel fuel composition to inhibit the formation of an emulsion
  • the quaternary ammonium salt additive (i) is formed by the reaction of a quaternising agent which is not an ester and a compound formed by the reaction of a hydrocarbyl-substituted acylating agent and an amine of formula (B1) or (B2): wherein R 2 and R 3 are the same or different alkyl, alkenyl or aryl groups having from 1 to 22 carbon atoms; X is a bond or alkylene group having from 1 to 20 carbon atoms; n is from 0 to 20; m is from 1 to 5; and R 4 is hydrogen or a C 1 to C 22 alkyl group; and wherein the Mannich reaction product additive (ii) is the product of a Mannich
  • Additive compounds (i) may be referred to herein as "the quaternary ammonium salt additives" or additive (i).
  • Additive compounds (ii) may be referred to herein as "the Mannich additives" or additive (ii).
  • the quaternising agents used to form the quaternary ammonium salt additives of the present invention are not esters.
  • RCOOR 1 in which R is an optionally substituted alkyl, alkenyl, aryl or alkylaryl group and R 1 is a C 1 to C 22 alkyl, aryl or alkylaryl group.
  • the quaternising agent may suitably be selected from dialkyl sulfates, benzyl halides, hydrocarbyl substituted carbonates, hydrocarbyl susbsituted epoxides in combination with an acid, alkyl halides, alkyl sulfonates, sultones, hydrocarbyl substituted phosphates, hydrocarbyl substituted borates, alkyl nitrites, alkyl nitrates, hydroxides, N-oxides or mixtures thereof.
  • the quaternary ammonium salt may be prepared from, for example, an alkyl or benzyl halide (especially a chloride) and then subjected to an ion exchange reaction to provide a different anion as part of the quaternary ammonium salt.
  • an alkyl or benzyl halide especially a chloride
  • Such a method may be suitable to prepare quaternary ammonium hydroxides, alkoxides, nitrites or nitrates.
  • Preferred quaternising agents include dialkyl sulfates, benzyl halides, hydrocarbyl substituted carbonates, hydrocarbyl susbsituted epoxides in combination with an acid, alkyl halides, alkyl sulfonates, sultones, hydrocarbyl substituted phosphates, hydrocarbyl substituted borates, N-oxides or mixtures thereof.
  • Suitable dialkyl sulfates for use herein include those including alkyl groups having 1 to 10, preferably 1 to 4 carbons atoms in the alkyl chain.
  • a preferred compound is dimethyl sulfate.
  • Suitable benzyl halides include chlorides, bromides and iodides.
  • the phenyl group may be optionally substituted, for example with one or more alkyl or alkenyl groups, especially when the chlorides are used.
  • a preferred compound is benzyl bromide.
  • Suitable hydrocarbyl substituted carbonates may include two hydrocarbyl groups, which may be the same or different.
  • Each hydrocarbyl group may contain from 1 to 50 carbon atoms, preferably from 1 to 20 carbon atoms, more preferably from 1 to 10 carbon atoms, suitably from 1 to 5 carbon atoms.
  • Preferably the or each hydrocarbyl group is an alkyl group.
  • Preferred compounds of this type include diethyl carbonate and dimethyl carbonate.
  • Suitable hydrocarbyl susbsituted epoxides have the formula: wherein each of R 1 , R 2 , R 3 and R 4 is independently hydrogen or a hydrocarbyl group having 1 to 50 carbon atoms.
  • suitable epoxides include ethylene oxide, propylene oxide, butylene oxide, styrene oxide and stillbene oxide.
  • the hydrocarbyl epoxides are used as quaternising agents in combination with an acid.
  • the hydrocarbyl substituted acylating agent is a dicarboxylic acylating agent no separate acid needs to be added. However in other embodiments an acid such as acetic acid may be used.
  • Particularly preferred epoxides are propylene oxide and styrene oxide.
  • Suitable alkyl halides for use herein include chlorides, bromides and iodides.
  • Suitable alkyl sulfonates include those having 1 to 20, preferably 1 to 10, more preferably 1 to 4 carbon atoms.
  • Suitable sultones include propane sultone and butane sultone.
  • Suitable hydrocarbyl substituted phosphates include dialkyl phosphates, trialkyl phosphates and O,O-dialkyl dithiophospates.
  • Preferred alkyl groups have 1 to 12 carbon atoms.
  • Suitable hydrocarbyl substituted borate groups include alkyl borates having 1 to 12 carbon atoms.
  • Preferred alkyl nitrites and alkyl nitrates have 1 to 12 carbon atoms.
  • the quaternising agent is selected from dialkyl sulfates, benzyl halides, hydrocarbyl substituted carbonates, hydrocarbyl susbsituted epoxides in combination with an acid, and mixtures thereof.
  • Especially preferred quaternising agents for use herein are hydrocarbyl substituted epoxides in combination with an acid.
  • the acid group is present as a part of the structure of the compound which is being quaternised.
  • the quaternising agent is reacted with a compound formed by the reaction of a hydrocarbyl substituted acylating agent and an amine of formula (B1) or (B2).
  • R 4 is preferably hydrogen or a C 1 to C 16 alkyl group, preferably a C 1 to C 10 alkyl group, more preferably a C 1 to C 6 alkyl group.
  • R 4 is alkyl it may be straight chained or branched. It may be substituted for example with a hydroxy or alkoxy substituent.
  • R 4 is not a substituted alkyl group. More preferably R 4 is selected from hydrogen, methyl, ethyl, propyl, butyl and isomers thereof. Most preferably R 4 is hydrogen.
  • n is preferably from 0 to 15, preferably 0 to 10, more preferably from 0 to 5. Most preferably n is 0 and the compound of formula (B2) is an alcohol.
  • hydrocarbyl substituted acylating agent is reacted with a diamine compound of formula (B1).
  • R 2 and R 3 are the same or different alkyl, alkenyl or aryl groups having from 1 to 22 carbon atoms. In some embodiments R 2 and R 3 may be joined together to form a ring structure, for example a piperidine or imidazole moiety. R 2 and R 3 may be branched alkyl or alkenyl groups. Each may be substituted, for example with a hydroxy or alkoxy substituent.
  • R 2 and R 3 may each independently be a C 1 to C 16 alkyl group, preferably a C 1 to C 10 alkyl group.
  • R 2 and R 3 may independently be methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl, or an isomer of any of these.
  • R 2 and R 3 is each independently C 1 to C 4 alkyl.
  • R 2 is methyl.
  • R 3 is methyl.
  • X is a bond or alkylene group having from 1 to 20 carbon atoms. In preferred embodiments when X alkylene group this group may be straight chained or branched.
  • the alkylene group may include a cyclic structure therein. It may be optionally substituted, for example with a hydroxy or alkoxy substituent.
  • X is preferably an alkylene group having 1 to 16 carbon atoms, preferably 1 to 12 carbon atoms, more preferably 1 to 8 carbon atoms, for example 2 to 6 carbon atoms or 2 to 5 carbon atoms. Most preferably X is an ethylene, propylene or butylene group, especially a propylene group.
  • Examples of compounds of formula (B1) suitable for use herein include 1-aminopiperidine, 1-(2-aminoethyl)piperidine, 1- (3-aminopropyl)-2-pipecoline, 1-methyl-(4-methylamino)piperidine, 4-(1-pyrrolidinyl)piperidine, 1-(2-aminoethyl)pyrrolidine, 2-(2-aminoethyl)-1-methylpyrrolidine, N,N-diethylethylenediamine, N,N-dimethylethylenediamine, N,N-dibutylethylenediamine, N,N-diethyl-I,3-diaminopropane, N,N-dimethyl-1,3-diaminopropane, N,N,N'-trimethylethylenediamine, N,N-dimethyl-N'-ethylethylenediamine, N,N-diethyl-N'-methylethylenediamine, N,N,N'
  • the compound of formula (B1) is selected from from N,N-dimethyl-1,3-diaminopropane, N,N-diethyl-1,3- diaminopropane, N,N-dimethylethylenediamine, N,N-diethylethylenediamine, N,N-dibutylethylenediamine, or combinations thereof.
  • Examples of compounds of formula (B2) suitable for use herein include alkanolamines including but not limited to triethanolamine, N,N-dimethylaminopropanol, N,N-diethylaminopropanol, N,N-diethylaminobutanol, triisopropanolamine, 1-[2-hydroxyethyl]piperidine, 2-[2-(dimethylamine)ethoxy]-ethanol, N-ethyldiethanolamine, N-methyldiethanolamine, N-butyldiethanolamine, N,N-diethylaminoethanol, N,N-dimethyl aminoethanol, 2-dimethylamino-2-methyl-1-propanol.
  • alkanolamines including but not limited to triethanolamine, N,N-dimethylaminopropanol, N,N-diethylaminopropanol, N,N-diethylaminobutanol, triisopropanolamine, 1-[2-
  • the compound of formula (B2) is selected from Triisopropanolamine, 1-[2-hydroxyethyl]piperidine, 2-[2-(dimethylamine)ethoxy]-ethanol, N-ethyldiethanolamine, N-methyldiethanolamine, N-butyldiethanolamine, N,N-diethylaminoethanol, N,N-dimethylaminoethanol, 2-dimethylamino-2-methyl-1-propanol, or combinations thereof.
  • An especially preferred compound of formula (B1) is dimethylaminopropylamine.
  • the amine of formula (B1) or (B2) is reacted with a hydrocarbyl substituted acylating agent.
  • the hydrocarbyl substituted acylating agent may be based on a hydrocarbyl substituted mono-di- or polycarboxylic acid or a reactive equivalent thereof.
  • the hydrocarbyl substituted acylating agent is a hydrocarbyl substituted succinic acid compound such as a succinic acid or succinic anhydride.
  • the hydrocarbyl substituent preferably comprises at least 10, more preferably at least 12, for example 30 or 50 carbon atoms. It may comprise up to about 200 carbon atoms.
  • the hydrocarbyl substituent has a number average molecular weight (Mn) of between 170 to 2800, for example from 250 to 1500, preferably from 500 to 1500 and more preferably 500 to 1100. An Mn of 700 to 1300 is especially preferred.
  • the hydrocarbyl based substituents may be made from homo- or interpolymers (e.g. copolymers, terpolymers) of mono- and di-olefins having 2 to 10 carbon atoms, for example ethylene, propylene, butane-1, isobutene, butadiene, isoprene, 1-hexene, 1-octene, etc. Preferably these olefins are 1-monoolefins.
  • the hydrocarbyl substituent may also be derived from the halogenated (e.g. chlorinated or brominated) analogs of such homo- or interpolymers.
  • the substituent may be made from other sources, for example monomeric high molecular weight alkenes (e.g. 1-tetra-contene) and chlorinated analogs and hydrochlorinated analogs thereof, aliphatic petroleum fractions, for example paraffin waxes and cracked and chlorinated analogs and hydrochlorinated analogs thereof, white oils, synthetic alkenes for example produced by the Ziegler-Natta process (e.g. poly(ethylene) greases) and other sources known to those skilled in the art. Any unsaturation in the substituent may if desired be reduced or eliminated by hydrogenation according to procedures known in the art.
  • monomeric high molecular weight alkenes e.g. 1-tetra-contene
  • chlorinated analogs and hydrochlorinated analogs thereof aliphatic petroleum fractions, for example paraffin waxes and cracked and chlorinated analogs and hydrochlorinated analogs thereof, white oils
  • synthetic alkenes for example produced by the Ziegler-Natta process (e
  • hydrocarbyl denotes a group having a carbon atom directly attached to the remainder of the molecule and having a predominantly aliphatic hydrocarbon character.
  • Suitable hydrocarbyl based groups may contain non-hydrocarbon moieties. For example they may contain up to one non-hydrocarbyl group for every ten carbon atoms provided this non-hydrocarbyl group does not significantly alter the predominantly hydrocarbon character of the group.
  • groups which include for example hydroxyl, oxygen, halo (especially chloro and fluoro), alkoxyl, alkyl mercapto, alkyl sulphoxy, etc.
  • Preferred hydrocarbyl based substituents are purely aliphatic hydrocarbon in character and do not contain such groups.
  • the hydrocarbyl-based substituents are preferably predominantly saturated, that is, they contain no more than one carbon-to-carbon unsaturated bond for every ten carbon-to-carbon single bonds present. Most preferably they contain no more than one carbon-to-carbon unsaturated bond for every 50 carbon-to-carbon bonds present.
  • hydrocarbyl-based substituents are poly-(isobutene)s known in the art.
  • the hydrocarbyl substituted acylating agent is a polyisobutenyl substituted succinic anhydride.
  • polyisobutenyl substituted succinic anhydrides PIBSA
  • Suitable processes include thermally reacting polyisobutenes with maleic anhydride (see for example US-A-3,361,673 and US-A-3,018,250 ), and reacting a halogenated, in particular a chlorinated, polyisobutene (PIB) with maleic anhydride (see for example US-A-3,172,892 ).
  • PIB chlorinated, polyisobutene
  • the polyisobutenyl succinic anhydride can be prepared by mixing the polyolefin with maleic anhydride and passing chlorine through the mixture (see for example GB-A-949,981 ).
  • polyisobutenes and so-called "highly-reactive" polyisobutenes are suitable for use in preparing additive (i) of the present invention.
  • Highly reactive polyisobutenes in this context are defined as polyisobutenes wherein at least 50%, preferably 70% or more, of the terminal olefinic double bonds are of the vinylidene type as described in EP0565285 .
  • Particularly preferred polyisobutenes are those having more than 80 mol% and up to 100% of terminal vinylidene groups such as those described in EP1344785 .
  • hydrocarbyl groups include those having an internal olefin for example as described in the applicant's published application WO2007/015080 .
  • An internal olefin as used herein means any olefin containing predominantly a non-alpha double bond, that is a beta or higher olefin.
  • such materials are substantially completely beta or higher olefins, for example containing less than 10% by weight alpha olefin, more preferably less than 5% by weight or less than 2% by weight.
  • Typical internal olefins include Neodene 151810 available from Shell.
  • Internal olefins are sometimes known as isomerised olefins and can be prepared from alpha olefins by a process of isomerisation known in the art, or are available from other sources. The fact that they are also known as internal olefins reflects that they do not necessarily have to be prepared by isomerisation.
  • Some preferred acylating agents for use in the preparation of the quaternary ammonium salt additives of the present invention are polyisobutene-substituted succinic acids or succinic anhydrides.
  • a compound of formula (B2) is reacted with a succinic acylating agent the resulting product is a succinic ester.
  • a succinic acylating agent is reacted with a compound of formula (B1) in which R 4 is hydrogen the resulting product may be a succinimide or a succinamide.
  • a succinic acylating agent is reacted with a compound of formula (B1) in which R 4 is not hydrogen the resulting product is an amide.
  • reaction product of the hydrocarbyl substituted acylating agent and the amine of formula (B1) or (B2) is an amide or an ester.
  • the reaction product of the hydrocarbyl substituted acylating agent and the amine of formula (B1) or (B2) also has at least one remaining carboxylic acid group.
  • This may be achieved by choosing hydrocarbyl substituted acylating agents having di or polycarboxylic acids or reactive equivalents thereof and by choosing suitable molar ratios of amines of formula (B1) or (B2).
  • amides prepared from amines of formula (B2) where R 4 is hydrogen it may also be necessary to control the reaction conditions to avoid forming imides. Such techniques are within the capability of someone of ordinary skill in the art.
  • succinic esters include the monoester compounds having the general formula (C1) and the diester compounds having the general formula (C2); succinimides have the general formula (C3); and succinamides include the monoamide compounds having the general formula (C4) and the diamide compounds having have the general formula (C5):
  • the quaternary ammonium salt additives of the present invention are salts of tertiary amines prepared from dimethylamino propylamine and a polyisobutylene-substituted succinic anhydride.
  • the average molecular weight of the polyisobutylene substituent is preferably from 700 to 1300, more preferably from 900 to 1100.
  • the quaternary ammonium salt additives of the present invention may be prepared by any suitable method. Such methods will be known to the person skilled in the art and are exemplified herein. Typically the quaternary ammonium salt additives will be prepared by heating the quaternising agent and a compound prepared by the reaction of a hydrocarbyl substituted acylating agent with an amine of formula (B1) or (B2) in an approximate 1:1 molar ratio, optionally in the presence of a solvent. The resulting crude reaction mixture may be added directly to a diesel fuel, optionally following removal of solvent. Any by-products or residual starting materials still present in the mixture have not been found to cause any detriment to the performance of the additive. Thus the present invention may provide a diesel fuel composition comprising the reaction product of a quaternising agent and the reaction product of a hydrocarbyl substituted acylating agent and an amine formula (B1) or (B2).
  • Particularly preferred quaternary ammonium salts of the present invention are the reaction product of a polyisobutenyl succinic acylating agent with dimethylaminopropylamine (N,N dimethyl 1,3 propane diamine) to form the half amide, half acid and then quaternised using propylene oxide.
  • composition of the present invention further comprises a second additive (ii) which is the product of a Mannich reaction between:
  • aldehyde component (a) of the Mannich additive may be used as aldehyde component (a) of the Mannich additive.
  • the aldehyde component (a) is an aliphatic aldehyde.
  • the aldehyde has 1 to 10 carbon atoms, preferably 1 to 6 carbon atoms, more preferably 1 to 3 carbon atoms. Most preferably the aldehyde is formaldehyde.
  • Amine component (b) of the Mannich additive may be at least one amino or polyamino compound having at least one NH group.
  • Suitable amino compounds include primary or secondary monoamines having hydrocarbon substituents of 1 to 30 carbon atoms or hydroxyl-substituted hydrocarbon substituents of 1 to about 30 carbon atoms.
  • the amine component (b) is a polyamine.
  • Polyamines may be selected from any compound including two or more amine groups.
  • the polyamine is a (poly)alkylene polyamine (by which is meant an alkylene polyamine or a polyalkylene polyamine; including in each case a diamine, within the meaning of "polyamine”).
  • the polyamine is a (poly)alkylene polyamine in which the alkylene component has 1 to 6, preferably 1 to 4, most preferably 2 to 3 carbon atoms.
  • the polyamine is a (poly) ethylene polyamine (that is, an ethylene polyamine or a polyethylene polyamine).
  • the polyamine has 2 to 15 nitrogen atoms, preferably 2 to 10 nitrogen atoms, more preferably 2 to 8 nitrogen atoms.
  • the polyamine component (b) includes the moiety R 1 R 2 NCHR 3 CHR 4 NR 5 R 6 wherein each of R 1 , R 2 R 3 , R 4 , R 5 and R 6 is independently selected from hydrogen, and an optionally substituted alkyl, alkenyl, alkynyl, aryl, alkylaryl or arylalkyl substituent.
  • polyamine reactants used to make the Mannich reaction products of the present invention preferably include an optionally substituted ethylene diamine residue.
  • R 1 and R 2 are hydrogen.
  • both of R 1 and R 2 are hydrogen.
  • R 1 , R 2 , R 5 and R 6 are hydrogen.
  • R 3 and R 4 are hydrogen.
  • each of R 3 and R 4 is hydrogen.
  • R 3 is hydrogen and R 4 is alkyl, for example C 1 to C 4 alkyl, especially methyl.
  • R 5 and R 6 is an optionally substituted alkyl, alkenyl, alkynyl, aryl, alkylaryl or arylalkyl substituent.
  • each is independently selected from an optionally substituted alkyl, alkenyl, alkynyl, aryl, alkylaryl or arylalkyl moiety.
  • each is independently selected from hydrogen and an optionally substituted C(1-6) alkyl moiety.
  • each of R 1 , R 2 , R 3 , R 4 and R 5 is hydrogen and R 6 is an optionally substituted alkyl, alkenyl, alkynyl, aryl, alkylaryl or arylalkyl substituent.
  • R 6 is an optionally substituted C(1-6) alkyl moiety.
  • Such an alkyl moiety may be substituted with one or more groups selected from hydroxyl, amino (especially unsubstituted amino; -NH-, -NH 2 ), sulpho, sulphoxy, C(1-4) alkoxy, nitro, halo (especially chloro or fluoro) and mercapto.
  • heteroatoms incorporated into the alkyl chain, for example O, N or S, to provide an ether, amine or thioether.
  • R 1 , R 2 , R 3 , R 4 , R 5 or R 6 are hydroxy-C(1-4)alkyl and amino-(C(1-4)alkyl, especially HO-CH 2 -CH 2 - and H 2 N-CH 2 -CH 2 -.
  • the polyamine includes only amine functionality, or amine and alcohol functionalities.
  • the polyamine may, for example, be selected from ethylenediamine, diethylenetriamine, triethylenetetramine, tetraethylenepentamine, pentaethylene-hexamine, hexaethyleneheptamine, heptaethyleneoctamine, propane-1,2-diamine, 2(2-aminoethylamino)ethanol, and N,N-bis (2-aminoethyl) ethylenediamine (N(CH 2 CH 2 NH 2 ) 3 ). Most preferably the polyamine comprises tetraethylenepentamine or ethylenediamine.
  • the polyamines used to form the Mannich additives of the present invention may be straight chained or branched, and may include cyclic structures.
  • Phenol component (c) used to prepare the Mannich additives of the present invention may be substituted with 1 to 4 groups on the aromatic ring (in addition to the phenol OH).
  • it may be a tri- or di- substituted phenol.
  • Most preferably component (c) is a mono-substituted phenol. Substitution may be at the ortho, and/or meta, and/or para position(s).
  • Each phenol moiety may be ortho, meta or para substituted with the aldehyde/amine residue.
  • Compounds in which the aldehyde residue is ortho or para substituted are most commonly formed. Mixtures of compounds may result.
  • the starting phenol is para substituted and thus the ortho substituted product results.
  • the phenol may be substituted with any common group, for example one or more of an alkyl group, an alkenyl group, an alkynl group, a nitryl group, a carboxylic acid, an ester, an ether, an alkoxy group, a halo group, a further hydroxyl group, a mercapto group, an alkyl mercapto group, an alkyl sulphoxy group, a sulphoxy group, an aryl group, an arylalkyl group, a substituted or unsubstituted amine group or a nitro group.
  • an alkyl group an alkenyl group, an alkynl group, a nitryl group, a carboxylic acid, an ester, an ether, an alkoxy group, a halo group, a further hydroxyl group, a mercapto group, an alkyl mercapto group, an alkyl sulphoxy group, a sulphoxy group
  • the phenol includes at least one branched hydrocarbyl substituent.
  • the hydrocarbyl substituent may be optionally substituted with, for example, hydroxyl, halo, (especially chloro and fluoro), alkoxy, alkyl, mercapto, alkyl sulphoxy, aryl or amino residues.
  • the hydro carbyl group consists essentially of carbon and hydrogen atoms.
  • the substituted phenol may include an alkenyl or alkynyl residue including one or more double and/or triple bonds.
  • the hydrocarbyl-based substituents are preferably predominantly saturated, that is, they contain no more than one carbon-to-carbon unsaturated bond for every ten carbon-to-carbon single bonds present. Most preferably they contain no more than one carbon-to-carbon unsaturated bond for every 50 carbon-to-carbon bonds present.
  • component (c) is a monoalkyl phenol, especially a para-substituted monoalkyl phenol in which the alkyl chain of the substituent is branched.
  • phenol component (c) used to prepare Mannich reaction product additive (ii) includes a predominantly or completely saturated branched hydrocarbyl substituent.
  • this predominantly or completely saturated hydrocarbyl substituent is branched along the length of the chain.
  • branched along the length of the chain we mean that there are multiple branches from the main (or longest) chain.
  • a particular carbon atom in the main hydrocarbyl chain (which is preferably an alkylene chain) may have one or two branching hydrocarbyl groups.
  • branching hydrocarbyl groups we mean hydrocarbyl groups not forming part of the main chain but directly attached thereto.
  • the main hydrocarbyl chain may include the moiety -CHR 1 - or -CR 1 R 2 - wherein R 1 and R 2 are branching hydrocarbyl groups.
  • each branching hydrocarbyl group is an alkyl group, preferably a C 1 to C 4 alkyl group, for example propyl, ethyl or most preferably methyl.
  • phenol component (c) used to prepare Mannich reaction product additive (ii) includes a hydrocarbyl substituent which is substituted with methyl groups along the main chain thereof.
  • a hydrocarbyl substituent which is substituted with methyl groups along the main chain thereof.
  • branching points are substantially equally spaced along the main chain of the hydrocarbyl group of phenol component (c).
  • Component (c) used to prepare additive (ii) includes at least one branched hydrocarbyl substituent.
  • this is an alkyl substituent.
  • the hydrocarbyl substituent is derived from a polyalkene, suitably a polymer of a branched alkene, for example polyisobutene or polypropene.
  • component (c) used in the preparation of Mannich reaction product additive (ii) includes a poly(isobutene) derived substituent.
  • Mannich reaction product additives (ii) used in the present invention preferably include a hydrocarbyl chain having the repeating unit:
  • polyisobutenes and so-called "highly-reactive" polyisobutenes are suitable for use in preparing additive (ii) of the present invention.
  • Highly reactive polyisobutenes in this context are defined as polyisobutenes wherein at least 50%, preferably 70% or more, of the terminal olefinic double bonds are of the vinylidene type as described in EP0565285 .
  • Particularly preferred polyisobutenes are those having more than 80 mol% and up to 100% of terminal vinylidene groups such as those described in EP1344785 .
  • the hydrocarbyl substituent of component (c) has an average molecular weight of 200 to 3000. Preferably it has a molecular weight of at least 225, suitably at least 250, preferably at least 275, suitably at least 300, for example at least 325 or at least 350. In some embodiments the hydrocarbyl substituent of component (c) has an average molecular weight of at least 375, preferably at least 400, suitably at least 475, for example at least 500.
  • component (c) may include a hydrocarbyl substituent having an average molecular weight of up to 2800, preferably up to 2600, for example up to 2500 or up to 2400.
  • the hydrocarbyl substituent of component (c) has an average molecular weight of from 400 to 2500, for example from 450 to 2400, preferably from 500 to 1500, suitably from 550 to 1300.
  • hydrocarbyl substituent of component (c) has an average molecular weight of from 200 to 600.
  • hydrocarbyl substituent of component (c) has an average molecular weight of from 500 to 1000.
  • hydrocarbyl substituent of component (c) has an average molecular weight of from 700 to 1300.
  • hydrocarbyl substituent of component (c) has an average molecular weight of from 1000 to 2000.
  • the hydrocarbyl substituent of component (c) has an average molecular weight of from 1700 to 2600, for example 2000 to 2500.
  • Components (a), (b) and (c) used to prepare the Mannich product additives (ii) may each comprise a mixture of compounds and/or a mixture of isomers.
  • the Mannich additive is preferably the reaction product obtained by reacting components (a), (b) and (c) in a molar ratio of from 5:1:5 to 0.1:1:0.1, more preferably from 3:1:3 to 0.5:1:0.5.
  • components (a) and (b) are preferably reacted in a molar ratio of from 6:1 to 1:4 (aldehyde:amine), preferably from 4:1 to 1:2, more preferably from 3:1 to 1:1.
  • the molar ratio of component (a) to component (b) (aldehyde:amine) in the reaction mixture is preferably greater than 1:1, preferably at least 1.1:1, more preferably at least 1.3:1, suitably at least 1.5:1, for example at least 1.6:1.
  • the molar ratio of component (a) to component (b) (aldehyde:amine) in the reaction mixture is less than 3:1, preferably up to 2.7:1, more preferably up to 2.3:1, for example up to 2.1:1, or up to 2:1.
  • the molar ratio of component (a) to component (b) (aldehyde:amine) in the reaction mixture used to prepare the Mannich additive of the present invention is from 1.1:1 to 2.9:1, preferably from 1.3:1 to 2.7:1, preferably from 1.4:1 to 2.5:1, more preferably from 1.5:1 to 2.3:1, suitably from 1.6:1 to 2.2:1, for example from 1.7:1 to 2.1:1.
  • the molar ratio of component (a) to component (c) (aldehyde:phenol) in the reaction mixture is preferably from 5:1 to 1:4, preferably from 3:1 to 1:2, for example from 2:1 to 1:1.
  • the molar ratio of component (a) to component (c) (aldehyde:phenol) in the reaction mixture used to prepare the Mannich additive of the present invention is greater than 1:1; preferably at least 1.1:1; preferably at least 1.2:1 and more preferably at least 1.3:1.
  • the molar ratio of component (a) to component (c) is less than 2:1, preferably up to 1.9:1; more preferably up to 1.8:1 for example up to 1.7:1; more preferably up to 1.6:1.
  • the molar ratio of component (a) to component (c) (aldehyde:phenol) in the reaction mixture used to prepare the Mannich additive is from 1.05:1 to 1.95:1, preferably from 1.1:1 to 1.85:1, more preferably from 1.2:1 to 1.75:1, suitably from 1.25:1 to 1.65:, most preferably from 1.3:1 to 1.55 :1.
  • components (c) and (b) are preferably reacted in a molar ratio of from 6:1 to 1:4 (phenol : amine), preferably from 4:1 to 1:2, more preferably from 3:1 to 1:2 and more preferably from 2:1 to 1:2.
  • the molar ratio of component (c) to component (b) (phenol:amine) in the reaction mixture is 0.7:1 to 1.9: 1, preferably 0.8:1 to 1.8:1, preferably 0.9:1 to 1.7:1, preferably 1:1 to 1.6:1 preferably 1.1:1 to 1.5:1, preferably 1.2:1 to 1.4:1.
  • the molar ratio of component (c) to component (b) (phenol : amine) in the reaction mixture is greater than 0.5:1; preferably at least 0.8:1; preferably at least 0.9:1 and more preferably at least 1:1 for example at least 1.1:1.
  • the molar ratio of component (c) to component (b) (phenol:amine) in the reaction mixture is less than 2:1, preferably up to 1.9:1; more preferably up to 1.7:1 for example up to 1.6:1; more preferably up to 1.5:1.
  • the molar ratio of component (a) to component (b) is 2.2-1.01:1; the molar ratio of component (a) to component (c) is 1.99-1.01:1 and the molar ratio of component (b) to component (c) is 1:1.01-1.99.
  • the molar ratio of component (a) to component (b) is 2-1.6:1
  • the molar ratio of component (a) to component (c) is 1.6-1.2:1
  • the molar ratio of component (b) to component (c) is 1:1.1-1.5.
  • Some preferred compounds used in the present invention are typically formed by reacting components (a), (b) and (c) in a molar ratio of 1.8 parts (a) ⁇ 0.3 parts (a), to 1 part (b), to 1.3 parts (c) ⁇ 0.3 parts (c); preferably 1.8 parts (a) ⁇ 0.1 parts (a), to 1 part (b), to 1.3 parts (c) ⁇ 0.1 parts (c); preferably approximately 1.8:1:1.3 (a : b : c).
  • Suitable treat rates of the quaternary ammonium salt additive and when present the Mannich additive will depend on the desired performance and on the type of engine in which they are used. For example different levels of additive may be needed to achieve different levels of performance.
  • the quaternary ammonium salt additive is present in the diesel fuel composition in an amount of from 1 to 10000ppm, preferably from 1 to 1000 ppm, more preferably from 5 to 500 ppm, suitably from 5 to 250 ppm, for example from 5 to 150ppm.
  • the Mannich additive when used is present in the diesel fuel composition in an amount of from 1 to 10000ppm, preferably from 1 to 1000 ppm, more preferably from 5 to 500 ppm, suitably from 5 to 250 ppm, for example from 5 to 150ppm.
  • the weight ratio of the quaternary ammonium salt additive to the Mannich additive is preferably from 1:10 to 10:1, preferably from 1:4 to 4:1, for example from 1:3 to 3:1.
  • fuels containing biodiesel or metals are known to cause fouling. Severe fuels, for example those containing high levels of metals and/or high levels of biodiesel may require higher treat rates of the quaternary ammonium salt additive and/or Mannich additive than fuels which are less severe.
  • the diesel fuel composition of the present invention may include one or more further additives such as those which are commonly found in diesel fuels. These include, for example, antioxidants, dispersants, detergents, metal deactivating compounds, wax anti-settling agents, cold flow improvers, cetane improvers, dehazers, stabilisers, demulsifiers, antifoams, corrosion inhibitors, lubricity improvers, dyes, markers, combustion improvers, metal deactivators, odour masks, drag reducers and conductivity improvers. Examples of suitable amounts of each of these types of additives will be known to the person skilled in the art.
  • the composition additionally comprises a dehazer/demulsifier.
  • Dehazer/demulsifiers are commercially available, for example from Nalco or Baker Hughes. Suitable compounds include, but are not limited to alkoxylated phenol formaldehyde polymers, alkylated phenols and resins derived therefrom, oxylated alkylphenolic resins, polyglycol esters, epoxides such as diepoxides, polyols, polyamines and ethylene oxide / propylene oxide block copolymers . Particularly preferred demulsifier/dehazers are a mixture of 2-4 different components comprising at least one alkoxylated phenol formaldehyde
  • the dehazer/demulsifier is suitably present in an amount of from 0.01 to 1000ppm, preferably from 0.1 to 500ppm, more preferably from 0.5 to 100ppm, for example from 1 to 50ppm.
  • the composition additionally comprises an antifoam additive.
  • antifoam additives are known to the person skilled in the art and include for example organomodified siloxanes, organo modified poly dimethyl siloxanes or polysilicone polyether copolymers. Examples of such compounds are available under the trade name SAGTM TP-317 or TP-325 from Momentive Perfomance Materials or Dow Corning® 2-2617 .
  • the antifoam additive is suitably present in an amount of from 0.01 to 1000ppm, preferably from 0.1 to 500ppm, more preferably from 0.5 to 100ppm, for example from 1 to 50ppm.
  • the compositon additionally comprises a detergent of the type formed by the reaction of a polyisobutene-substituted succinic acid-derived acylating agent and a polyethylene polyamine.
  • a detergent of the type formed by the reaction of a polyisobutene-substituted succinic acid-derived acylating agent and a polyethylene polyamine are, for example, described in WO2009/040583 .
  • diesel fuel we include any fuel suitable for use in a diesel engine, either for road use or non-road use. This includes, but is not limited to, fuels described as diesel, marine diesel, heavy fuel oil, industrial fuel oil etc.
  • the diesel fuel composition of the present invention may comprise a petroleum-based fuel oil, especially a middle distillate fuel oil.
  • Such distillate fuel oils generally boil within the range of from 110oC to 500oC, e.g. 150oC to 400oC.
  • the diesel fuel may comprise atmospheric distillate or vacuum distillate, cracked gas oil, or a blend in any proportion of straight run and refinery streams such as thermally and/or catalytically cracked and hydro-cracked distillates.
  • the diesel fuel composition of the present invention may comprise a Fischer-Tropsch fuel. It may comprise non-renewable Fischer-Tropsch fuels such as those described as GTL (gas-to-liquid) fuels, CTL (coal-to-liquid) fuels and OTL (oil sands-to-liquid).
  • GTL gas-to-liquid
  • CTL coal-to-liquid
  • OTL oil sands-to-liquid
  • the diesel fuel composition of the present invention may comprise a renewable fuel such as a biofuel composition or biodiesel composition.
  • the diesel fuel composition may comprise 1st generation biodiesel.
  • First generation biodiesel contains esters of, for example, vegetable oils, animal fats and used cooking fats. This form of biodiesel may be obtained by transesterification of oils, for example rapeseed oil, soybean oil, safflower oil, palm 25 oil, corn oil, peanut oil, cotton seed oil, tallow, coconut oil, physic nut oil (Jatropha), sunflower seed oil, used cooking oils, hydrogenated vegetable oils or any mixture thereof, with an alcohol, usually a monoalcohol, in the presence of a catalyst.
  • oils for example rapeseed oil, soybean oil, safflower oil, palm 25 oil, corn oil, peanut oil, cotton seed oil, tallow, coconut oil, physic nut oil (Jatropha), sunflower seed oil, used cooking oils, hydrogenated vegetable oils or any mixture thereof, with an alcohol, usually a monoalcohol, in the presence of a catalyst.
  • the diesel fuel composition may comprise second generation biodiesel.
  • Second generation biodiesel is derived from renewable resources such as vegetable oils and animal fats and processed, often in the refinery, often using hydroprocessing such as the H-Bio process developed by Petrobras.
  • Second generation biodiesel may be similar in properties and quality to petroleum based fuel oil streams, for example renewable diesel produced from vegetable oils, animal fats etc. and marketed by ConocoPhillips as Renewable Diesel and by Neste as NExBTL.
  • the diesel fuel composition of the present invention may comprise third generation biodiesel.
  • Third generation biodiesel utilises gasification and Fischer-Tropsch technology including those described as BTL (biomass-to-liquid) fuels.
  • BTL biomass-to-liquid
  • Third generation biodiesel does not differ widely from some second generation biodiesel, but aims to exploit the whole plant (biomass) and thereby widens the feedstock base.
  • the diesel fuel composition may contain blends of any or all of the above diesel fuel compositions.
  • the diesel fuel composition comprises a Fischer Tropsch fuel and/or biodiesel.
  • the diesel fuel composition of the present invention may be a blended diesel fuel comprising bio-diesel.
  • the bio-diesel may be present in an amount of, for example up to 0.5%, up to 1%, up to 2%, up to 3%, up to 4%, up to 5%, up to 10%, up to 20%, up to 30%, up to 40%, up to 50%, up to 60%, up to 70%, up to 80%, up to 90%, up to 95% or up to 99%.
  • the composition comprises from 1 to 20 wt%, biodiesel, preferably from 5 to 10 wt%.
  • the diesel fuel composition may comprise a secondary fuel, for example ethanol.
  • a secondary fuel for example ethanol.
  • the diesel fuel composition does not contain ethanol.
  • the diesel fuel composition of the present invention may contain a relatively high sulphur content, for example greater than 0.05% by weight, such as 0.1% or 0.2%.
  • the diesel fuel has a sulphur content of at most 0.05% by weight, more preferably of at most 0.035% by weight, especially of at most 0.015%.
  • Fuels with even lower levels of sulphur are also suitable such as, fuels with less than 50 ppm sulphur by weight, preferably less than 20 ppm, for example 10 ppm or less.
  • metal-containing species will be present as a contaminant, for example through the corrosion of metal and metal oxide surfaces by acidic species present in the fuel or from lubricating oil.
  • fuels such as diesel fuels routinely come into contact with metal surfaces for example, in vehicle fuelling systems, fuel tanks, fuel transportation means etc.
  • metal-containing contamination may comprise transition metals such as zinc, iron and copper; group I or group II metals such as sodium; and other metals such as lead.
  • metal-containing fuel-borne catalyst species may be added to aid with the regeneration of particulate traps.
  • metal-containing fuel-borne catalyst species may be added to aid with the regeneration of particulate traps.
  • Such catalysts are often based on metals such as iron, cerium, Group I and Group II metals e.g., calcium and strontium, either as mixtures or alone. Also used are platinum and manganese. The presence of such catalysts may also give rise to injector deposits when the fuels are used in diesel engines having high pressure fuel systems.
  • Metal-containing contamination depending on its source, may be in the form of insoluble particulates or soluble compounds or complexes.
  • Metal-containing fuel-borne catalysts are often soluble compounds or complexes or colloidal species.
  • the metal-containing species comprises a fuel-borne catalyst.
  • the metal-containing species comprises zinc.
  • the diesel fuel composition of the invention comprises a fuel-borne catalyst which includes a metal selected from iron, cerium, group I and group II metals, platinum, manganese and mixtures thereof.
  • a fuel-borne catalyst which includes a metal selected from iron, cerium, group I and group II metals, platinum, manganese and mixtures thereof.
  • Preferred group I and group II metals include calcium and strontium.
  • the amount of metal-containing species in the diesel fuel is between 0.1 and 50 ppm by weight, for example between 0.1 and 10 ppm by weight, based on the weight of the diesel fuel.
  • the fuel compositions of the present invention show improved performance when used in diesel engines having high pressure fuel systems compared with diesel fuels of the prior art.
  • an additive package which upon addition to a diesel fuel provides a fuel composition as defined in relation to the first aspect.
  • the additive package may comprise a mixture of the quaternary ammonium salt additive, the Mannich additive and optionally further additives, for example those described above.
  • the additive package may comprise a solution of additives, suitably in a mixture of hydrocarbon solvents for example aliphatic and/or aromatic solvents; and/or oxygenated solvents for example alcohols and/or ethers.
  • Disclosed herein is a method of operating a diesel engine, the method comprising combusting in the engine a fuel composition as defined in relation to the first aspect.
  • quaternary ammonium salt additive i
  • a Mannich reaction product additive ii
  • the improvement in performance may be achieved by the reduction or the prevention of the formation of deposits in a diesel engine. This may be regarded as an improvement in "keep clean" performance.
  • the present invention may provide a method of reducing or preventing the formation of deposits in a diesel engine by combusting in said engine a composition of the first aspect.
  • the improvement in performance may be achieved by the removal of existing deposits in a diesel engine. This may be regarded as an improvement in "clean up" performance.
  • the present invention may provide a method of removing deposits from a diesel engine by combusting in said engine fuel a composition as defined in relation to the first aspect.
  • composition described in relation to the first aspect of the present invention may be used to provide an improvement in "keep clean” and “clean up” performance.
  • a quaternary ammonium salt additive optionally in combination with a Mannich additive, in a diesel fuel composition to improve the engine performance of a diesel engine when using said diesel fuel composition wherein the diesel engine has a high pressure fuel system.
  • Modern diesel engines having a high pressure fuel system may be characterised in a number of ways. Such engines are typically equipped with fuel injectors having a plurality of apertures, each aperture having an inlet and an outlet.
  • Such modern diesel engines may be characterised by apertures which are tapered such that the inlet diameter of the spray-holes is greater than the outlet diameter.
  • Such modern engines may be characterised by apertures having an outlet diameter of less than 500 ⁇ m, preferably less than 200 ⁇ m, more preferably less than 150 ⁇ m, preferably less than 100 ⁇ m, most preferably less than 80 ⁇ m or less.
  • Such modern diesel engines may be characterised by apertures where an inner edge of the inlet is rounded.
  • Such modern diesel engines may be characterised by the injector having more than one aperture, suitably more than 2 apertures, preferably more than 4 apertures, for example 6 or more apertures.
  • Such modern diesel engines may be characterised by an operating tip temperature in excess of 250°C.
  • Such modern diesel engines may be characterised by a fuel pressure of more than 1350 bar, preferably more than 1500 bar, more preferably more than 2000 bar.
  • the use of the present invention preferably improves the performance of an engine having one or more of the above-described characteristics.
  • the present invention is particularly useful in the prevention or reduction or removal of deposits on injectors of engines operating at high pressures and temperatures in which fuel may be recirculated and which comprise a plurality of fine apertures through which the fuel is delivered to the engine.
  • the present invention finds utility in engines for heavy duty vehicles and passenger vehicles. Passenger vehicles incorporating a high speed direct injection (or HSDI) engine may for example benefit from the present invention.
  • HSDI high speed direct injection
  • the diesel fuel compositions of the present invention may also provide improved performance when used with traditional diesel engines.
  • the improved performance is achieved when using the diesel fuel compositions in modern diesel engines having high pressure fuel systems and when using the compositions in traditional diesel engines. This is important because it allows a single fuel to be provided that can be used in new engines and older vehicles.
  • the improvement in performance of the diesel engine system may be measured by a number of ways. Suitable methods will depend on the type of engine and whether "keep clean” and/or “clean up” performance is measured.
  • One of the ways in which the improvement in performance can be measured is by measuring the power loss in a controlled engine test.
  • An improvement in "keep clean” performance may be measured by observing a reduction in power loss compared to that seen in a base fuel.
  • “Clean up” performance can be observed by an increase in power when diesel fuel compositions of the invention are used in an already fouled engine.
  • the improvement in performance of the diesel engine having a high pressure fuel system may be measured by an improvement in fuel economy.
  • the present invention may also improve the performance of the engine by reducing, preventing or removing deposits in the vehicle fuel filter.
  • the level of deposits in a vehicle fuel filter may be measured quantitatively or qualitatively. In some cases this may only be determined by inspection of the filter once the filter has been removed. In other cases, the level of deposits may be estimated during use.
  • a fuel filter which may be visually inspected during use to determine the level of solids build up and the need for filter replacement.
  • a filter canister within a transparent housing allowing the filter, the fuel level within the filter and the degree of filter blocking to be observed.
  • Using the fuel compositions of the present invention may result in levels of deposits in the fuel filter which are considerably reduced compared with fuel compositions not of the present invention. This allows the filter to be changed much less frequently and can ensure that fuel filters do not fail between service intervals. Thus the use of the compositions of the present invention may lead to reduced maintenance costs.
  • the occurrence of deposits in a fuel filter may be inhibited or reduced. Thus a "keep clean” performance may be observed. In some embodiments existing deposits may be removed from a fuel filter. Thus a “clean up” performance may be observed.
  • Improvement in performance may also be assessed by considering the extent to which the use of the fuel compositions of the invention reduce the amount of deposit on the injector of an engine. For “keep clean” performance a reduction in occurrence of deposits would be observed. For “clean up” performance removal of existing deposits would be observed.
  • Direct measurement of deposit build up is not usually undertaken, but is usually inferred from the power loss or fuel flow rates through the injector.
  • the present invention may improve performance of the engine by reducing, preventing or removing deposits including gums and lacquers within the injector body.
  • CEC F-98-08 the industry body known as CEC
  • the test is based on a Peugeot DW10 engine using Euro 5 injectors, and will hereinafter be referred to as the DW10 test. It will be further described in the context of the examples (see example 9).
  • the use of the fuel composition of the present invention leads to reduced deposits in the DW10 test.
  • a reduction in the occurrence of deposits is preferably observed.
  • For "clean up” performance removal of deposits is preferably observed.
  • the DW10 test is used to measure the power loss in modern diesel engines having a high pressure fuel system.
  • a fuel composition of the present invention may provide a "keep clean" performance in modern diesel engines, that is the formation of deposits on the injectors of these engines may be inhibited or prevented.
  • this performance is such that a power loss of less than 5%, preferably less than 2% is observed after 32 hours as measured by the DW10 test.
  • a fuel composition of the present invention may provide a "clean up" performance in modern diesel engines, that is deposits on the injectors of an already fouled engine may be removed.
  • this performance is such that the power of a fouled engine may be returned to within 1% of the level achieved when using clean injectors within 32 hours as measured in the DW10 test.
  • Preferably rapid "clean-up" may be achieved in which the power is returned to within 1% of the level observed using clean injectors within 10 hours, preferably within 8 hours, suitably within 6 hours, preferably within 4 hours, more preferably within 2 hours.
  • Clean injectors can include new injectors or injectors which have been removed and physically cleaned, for example in an ultrasound bath.
  • a fuel composition of the present invention may provide a "keep clean" performance in traditional diesel engines, that is the formation of deposits on the injectors of these engines may be inhibited or prevented.
  • this performance is such that a flow loss of less than 50%, preferably less than 30% is observed after 10 hours as measured by the XUD-9 test.
  • a fuel composition of the present invention may provide a "clean up" performance in traditional diesel engines, that is deposits on the injectors of an already fouled engine may be removed.
  • this performance is such that the flow loss of a fouled engine may be increased by 10% or more within 10 hours as measured in the XUD-9 test.
  • composition of the present invention has also been found to be stable on storage.
  • compositions of the present invention have been found to have a reduced tendency to form emulsions compared with similar compositions of the prior art.
  • the present invention provides the use of a first additive (i) comprising a quaternary ammonium salt and a second additive (ii) comprising a Mannich reaction product as defined in relation to the first aspect to inhibit the formation of an emulsion in a diesel fuel composition.
  • an emulsion forms less readily and/or separates more easily compared to when similar engine performance additives of the prior art are used.
  • the present invention further provides the use of a Mannich reaction product (ii) as defined herein to improve the demulsification performance of a diesel fuel composition comprising a dehazer/demulsifier and a quaternary ammonium salt additive (i) as defined herein.
  • the time taken for fuel and water to separate once mixed is particularly important in ensuring the quality of fuel taken from storage tanks.
  • fresh fuel is added to a storage tank, if there is any emulsified fuel/water, then it would be unacceptable to supply that fuel to an end user until the fuel and water had separated.
  • the fuel clarity must be acceptable to the end user.
  • the interface condition and fuel water separation rating are particularly important for ensuring that microbial growth is minimised at the fuel / water interface.
  • Additive A a quaternary ammonium salt additive of the present invention was prepared as follows: A mixture of succinic anhydride prepared from 1000 Mn polyisobutylene (21425g) and diluent oil - pilot 900 (3781g) were heated with stirring to 110°C under a nitrogen atmosphere. Dimethylaminopropylamine (DMAPA, 2314g) was added slowly over 45 minutes maintaining batch temperature below 115°C. The reaction temperature was increased to 150°C and held for a further 3 hours. The resulting compound is a DMAPA succinimide.
  • DMAPA Dimethylaminopropylamine
  • This DMAPA succinimide was heated with styrene oxide (12.5g), acetic acid (6.25g) and methanol (43.4g) under reflux (approx 80°C) with stirring for 5 hours under a nitrogen atmosphere.
  • the mixture was purified by distillation (30°C, -1 bar) to give the styrene oxide quaternary ammonium salt as a water white distillate.
  • Additive B a Mannich reaction product additive of the prior art was prepared as follows: A reactor was charged with dodecylphenol (170.6g, 0.65 mol), ethylenediamine (30.1g, 0.5 mol) and Caromax 20 (123.9g). The mixture was heated to 95°C and formaldehyde solution, 37 wt% (73.8g, 0.9 mol) charged over 1 hour. The temperature was increased to 125°C for 3 hours and water removed. In this example the molar ratio of aldehyde (a) : amine (b) : phenol (c) was approximately 1.8:1:1.3.
  • a polyiosbutene-substituted phenol was prepared as follows: Polyisobutene having an average molecular wieght of 750 (450.3g, 0.53mol, 1 equiv) was heated to 45-50oC and then phenol (150.0g, 1.59mol, 3equivs) was added. The turbid mixture was stirred and boron trifluoride dietherate (15.0g , 0.10mol, 0.18equivs) was added in 2-3ml aliquots over approx two hoursto provide a clear orange liquid which was stirred at 45-50oC for 5 hours. Aqueous ammonia 35% (10.5g , 0.22moles) was then added and the reaction mixture stirred for 30mins.
  • Vacuum distillation provided 81.3g of distillate. This was stirred at 70oC in toluene (250.3g) for 5 mins, before adding 250.4g of water. The layers were separated and the toluene extract was washed twice more with water. Residual water and toluene removed under vacuum to provide the product as a viscous pale yellow liquid. (510.9g) having a toluene content of 2 wt% and a phenol content of less than 0.2wt%.
  • Additive C a Mannich additive of the present invention was prepared as follows: PIB 750 Phenol (a phenol having a polyisobutenyl substituent of average molecular weight 750) with a residual PIB content of 5 wt% (447.8g, 425.4g "active" PIB phenol, 0.50moles, 1.3equivs) was mixed with ethylenediamine (25.3g, 0.38moles, 1 equiv) and Caromax 20 solvent (225.6g). The homogenous mixture was heated to 90-95oC.
  • Demulsifier(1) A commercially available demulsifier/dehazer comprising a mixture of phenolic resins in aromatic solvent.
  • Antifoam (2) A commercially available antifoam additive comprising organomodified siloxanes in aromatic solvent.
  • Solvent (3) A commercially available blend of aromatic and aliphatic solvents
  • Diesel fuel compositions were prepared by adding the additive compositions listed in table 1 to aliquots all drawn from a common batch of RF06 base fuel, and containing 1 ppm zinc (as zinc neodecanoate). In each case a total additive treat rate of 350ppm was used.
  • Table 2 shows the specification for RF06 base fuel.
  • Table 2 Property Units Limits Method Min Max Cetane Number 52.0 54.0 EN ISO 5165 Density at 15°C kg/m 3 833 837 EN ISO 3675 Distillation 50% v/v Point °C 245 - 95% v/v Point °C 345 350 FBP °C - 370 Flash Point °C 55 - EN 22719 Cold Filter Plugging °C - -5 EN 116 Point Viscosity at 40°C mm 2 /sec 2.3 3.3 EN ISO 3104 Polycyclic Aromatic % m/m 3.0 6.0 IP 391 Hydrocarbons Sulphur Content mg/kg - 10 ASTM D 5453 Copper Corrosion - 1 EN ISO 2160 Conradson Carbon Residue on % m/m - 0.2 EN ISO 10370 10% Dist.
  • Diesel fuel compositions were prepared comprising the additive compositions listed in Table 1, added to aliquots all drawn from a common batch of a B7 reference fuel prepared from 93% RF06 base fuel and 7% of a biodiesel comprising rapeseed oil methyl ester. Again, a total additive treat rate of 350ppm was used.
  • This test is designed to evaluate the tendency of water and fuels to separate rather than form emulsions when they contain potential emulsion forming additives or components.
  • 80ml of fuel and 20ml of water are shaken together under controlled conditions and then allowed to stand for a period of time. After 5 minutes, the volume of the aqueous layer, the fuel clarity, the fuel water separation and the interface condition are rated according to standard definitions.
  • composition 3 gave significantly better performance than compositions 1 or 2.
  • the engine of the injector fouling test is the PSA DW10BTED4.
  • the engine characteristics are: Design: Four cylinders in line, overhead camshaft, turbocharged with EGR Capacity: 1998 cm 3
  • Combustion chamber Four valves, bowl in piston, wall guided direct injection Power: 100 kW at 4000 rpm Torque: 320 Nm at 2000 rpm
  • Injection system Common rail with piezo electronically controlled 6-hole injectors. Max. pressure: 1600 bar (1.6 x 10 8 Pa).
  • Proprietary design by SIEMENS VDO Emissions control Conforms with Euro IV limit values when combined with exhaust gas post-treatment system(DPF)
  • This engine was chosen as a design representative of the modern European high-speed direct injection diesel engine capable of conforming to present and future European emissions requirements.
  • the common rail injection system uses a highly efficient nozzle design with rounded inlet edges and conical spray holes for optimal hydraulic flow. This type of nozzle, when combined with high fuel pressure has allowed advances to be achieved in combustion efficiency, reduced noise and reduced fuel consumption, but are sensitive to influences that can disturb the fuel flow, such as deposit formation in the spray holes. The presence of these deposits causes a significant loss of engine power and increased raw emissions.
  • test injector design representative of anticipated Euro V injector technology. It is considered necessary to establish a reliable baseline of injector condition before beginning fouling tests, so a sixteen hour running-in schedule for the test injectors is specified, using non-fouling reference fuel.
  • the standard CEC F-98-08 test method consists of 32 hours engine operation corresponding to 4 repeats of steps 1-3 above, and 3 repeats of step 4. ie 56 hours total test time excluding warm ups and cool downs.
  • a second 32 hour cycle may then be run as a 'clean up' phase.
  • the dirty injectors from the first phase were kept in the engine and the fuel changed to RF-06 base fuel having added thereto 1ppm Zn (as neodecanoate) and the test additives.
  • Nozzle coking is the result of carbon deposits forming between the injector needle and the needle seat. Deposition of the carbon deposit is due to exposure of the injector needle and seat to combustion gases, potentially causing undesirable variations in engine performance.
  • the Peugeot XUD9 A/L engine is a 4 cylinder indirect injection Diesel engine of 1.9 litre swept volume, obtained from Peugeot Citroen Motors specifically for the CEC PF023 method.
  • the test engine is fitted with cleaned injectors utilising unflatted injector needles.
  • the airflow at various needle lift positions have been measured on a flow rig prior to test.
  • the engine is operated for a period of 10 hours under cyclic conditions.
  • the propensity of the fuel to promote deposit formation on the fuel injectors is determined by measuring the injector nozzle airflow again at the end of test, and comparing these values to those before test. The results are expressed in terms of percentage airflow reduction at various needle lift positions for all nozzles. The average value of the airflow reduction at 0.1mm needle lift of all four nozzles is deemed the level of injector coking for a given fuel.
  • a diesel fuel composition was prepared by adding 350 ppm of additive composition 3 described in example 5 to a base fuel having the specification defined in example 6. This fuel and a base fuel were tested in a Peugeot XUD9 A/L Engine according to the method described in example 10. The results are shown in table 7. Table 7 Additive Composition Treat rate, mg/kg % Flow Loss Basefuel - 76.8 Composition 3 350 2.3

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Claims (11)

  1. Verwendung eines ersten Additivs (i), das ein quaternäres Ammoniumsalz umfasst, und eines zweiten Additivs (ii), das ein Mannich-Reaktionsprodukt umfasst, in einer Dieselkraftstoffzusammensetzung zur Inhibierung der Bildung einer Emulsion; wobei das quaternäre Ammoniumsalz-Additiv (i) durch die Reaktion eines Quaternisierungsmittels, bei dem es sich nicht um einen Ester handelt, und einer durch die Reaktion eines hydrocarbylsubstituierten Acylierungsmittels und eines Amins der Formel (B1) oder (B2)
    Figure imgb0006
     gebildeten Verbindung gebildet wird, wobei R2 und R3 für gleiche oder verschiedene Alkyl-, Alkenyl- oder Arylgruppen mit 1 bis 22 Kohlenstoffatomen stehen; X für eine Bindung oder eine Alkylengruppe mit 1 bis 20 Kohlenstoffatomen steht; n für 0 bis 20 steht; m für 1 bis 5 steht und R4 für Wasserstoff oder eine C1- bis C22-Alkylgruppe steht; und wobei es sich bei dem Mannich-Reaktionsprodukt-Additiv (ii) um das Produkt einer Mannich-Reaktion zwischen
    (a) einem Aldehyd,
    (b) einem Amin und
    (c) einem substituierten Phenol
    handelt, wobei das Phenyl durch mindestens eine verzweigte Hydrocarbylgruppe mit einem Molekulargewicht zwischen 200 und 3000 substituiert ist.
  2. Verwendung nach Anspruch 1, wobei das Quaternisierungsmittel aus Dialkylsulfaten, Benzylhalogeniden, hydrocarbylsubstituierten Carbonaten, hydrocarbylsubstituierten Epoxiden in Kombination mit einer Säure, Alkylhalogeniden, Alkylsulfonaten, Sultonen, hydrocarbylsubstituierten Phosphaten, hydrocarbylsubstituierten Boraten, Alkylnitriten, Alkylnitraten, N-Oxiden oder Mischungen davon ausgewählt ist.
  3. Verwendung nach Anspruch 2, wobei das Quaternisierungsmittel aus Dialkylsulfaten, Benzylhalogeniden, hydrocarbylsubstituierten Carbonaten und hydrocarbylsubstituierten Epoxiden in Kombination mit einer Säure ausgewählt ist.
  4. Verwendung nach einem der vorhergehenden Ansprüche, wobei das hydrocarbylsubstituierte Acylierungsmittel mit einer Diaminverbindung der Formel (B1) umgesetzt wird.
  5. Verwendung nach einem der vorhergehenden Ansprüche, wobei es sich bei dem Additiv (i) um ein aus Dimethylaminopropylamin und einem polyisobutylensubstituierten Bernsteinsäureanhydrid hergestelltes Salz eines tertiären Amins handelt.
  6. Verwendung nach einem der vorhergehenden Ansprüche, wobei es sich bei der zur Herstellung von Additiv (ii) verwendeten Komponente (b) um ein (Poly)ethylenpolyamin handelt.
  7. Verwendung nach einem der vorhergehenden Ansprüche, wobei es sich bei der zur Herstellung von Additiv (ii) verwendeten Komponente (c) um ein polyisobutylensubstituiertes Phenol handelt.
  8. Verwendung nach einem der vorhergehenden Ansprüche, wobei bei der zur Herstellung des Mannich-Additivs verwendeten Reaktion das Molverhältnis von Komponente (a) zu Komponente (b) 2-1,4:1 beträgt, das Molverhältnis von Komponente (a) zu Komponente (c) 1,7-1,1:1 beträgt und das Molverhältnis von Komponente (b) zu Komponente (c) 1:1,1-1,7 beträgt.
  9. Verwendung nach einem der vorhergehenden Ansprüche, wobei der Dieselkraftstoff einen nicht erneuerbaren Fischer-Tropsch-Kraftstoff und/oder Biodiesel umfasst.
  10. Verwendung nach einem der vorhergehenden Ansprüche, wobei die Dieselkraftstoffzusammensetzungen ferner einen kraftstoffgetragenen Katalysator umfassen, der ein Metall enthält, das aus Eisen, Cer, Gruppe-I- und Gruppe-II-Metallen, Platin, Mangan und Mischungen davon ausgewählt ist.
  11. Verwendung eines Mannich-Reaktionsprodukts (ii) gemäß einem der vorhergehenden Ansprüche zur Verbesserung der gemäß ASTM D7451 gemessenen Demulgierungsleistung einer Dieselkraftstoffzusammensetzung, die einen Demulgator/Dehazer und ein quaternäres Ammoniumsalz-Additiv (i) gemäß einem der vorhergehenden Ansprüche umfasst.
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AU2012291816B2 (en) 2016-07-07
CN103987818A (zh) 2014-08-13
GB201113392D0 (en) 2011-09-21
EP2739708A1 (de) 2014-06-11
CA2843232A1 (en) 2013-02-07
AU2012291816A1 (en) 2014-02-13
CA2843232C (en) 2021-07-20
KR102035360B1 (ko) 2019-11-08
US20140157656A1 (en) 2014-06-12
US20180187115A1 (en) 2018-07-05
CN103987818B (zh) 2016-10-05
WO2013017886A1 (en) 2013-02-07
KR20140061425A (ko) 2014-05-21
MY169348A (en) 2019-03-21
BR112014002623A2 (pt) 2017-03-01
AR087453A1 (es) 2014-03-26

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