diesel fuel composition, additive package, method of operating a diesel engine and use of an additiv

专利摘要:
DIESEL FUEL COMPOSITION, ADDITIVE PACKAGE, METHOD OF OPERATING A DIESEL ENGINE AND USE OF AN ADDITIVE The present invention relates to a diesel fuel composition comprising a first additive (i) comprising an ammonium salt quaternary and a second additive (ii) comprising a Mannich reaction product; wherein the quaternary ammonium salt additive (i) is formed by the reaction of a compound of formula (A): (A) and a compound formed by the reaction of an acylating agent with substituted hydrocarbyl and an amine of formula (B1) or (B2): (B1) (B2) where R is an optionally substituted alkyl, alkenyl, aryl or alkylaryl group; R1 is a C1 to C22 alkyl, aryl or alkylaryl group; wherein R2 and R3 are the same or different alkyl, alkenyl or aryl groups having from 1 to 22 carbon atoms; X is an alkylene bond or group having 1 to 20 carbon atoms; n is 0 to 20; m is 1 to 5; and R4 is hydrogen or a C1 to C22 alkyl group; and where the additive of the Mannich reaction product (ii) is the product of a reaction (...).
公开号:BR112014002541B1
申请号:R112014002541-0
申请日:2012-08-02
公开日:2020-12-01
发明作者:Jacqueline Reid
申请人:Innospec Limited；
IPC主号:

专利说明:

[001] The present invention relates to fuel compositions and their additives. In particular, the invention relates to additives for diesel fuel compositions, especially those suitable for use in modern diesel engines with high pressure fuel systems.
[002] Due to consumer demand and legislation, diesel engines have recently become much more energy efficient, show improved performance and have reduced emissions.
[003] These improvements in performance and emissions were caused by improvements in the combustion process. In order to achieve the fuel atomization required for this improved combustion, fuel injection equipment has been developed that uses higher injection pressures and reduced fuel injector nozzle bore diameters. The fuel pressure in the injection nozzle is currently in excess of 1.5 x 108 Pa (1,500 bars). To achieve these pressures, the work that needs to be done on the fuel also increases the temperature of the fuel. These high pressures and temperatures can cause fuel degradation.
[004] Diesel engines that have high pressure fuel systems may include, but are not limited to heavy duty diesel engines and smaller diesel engines for passenger cars. Heavy-duty diesel engines can include very powerful engines like the MTU 4000 series diesel, which has 20-cylinder variants designed initially for ships and power generation with a power output of up to 4,300 kW or engines like the Renault dXi 7 which has 6 cylinders and a power output of about 240 kW. A typical passenger car diesel engine is the Peugeot DW10 which has 4 cylinders and a power output of 100 kW or less depending on the variant.
[005] In all diesel engines related to this invention, a common feature is a high pressure fuel system. Typically, pressures in excess of 1.35 x 108 Pa (1,350 bars) are used, but pressures of up to 2 x 108 Pa (2,000 bars) or more can often exist.
[006] Two non-limiting examples of such high pressure fuel systems are: the common tube type injection system, in which the fuel is compressed using a high pressure pump that supplies the fuel to the injection valves fuel through a common pipe; and the pump and nozzle injection system that integrates the high pressure pump and the fuel injection valve in one assembly, achieving the highest possible injection pressures that exceed 2 x 108 Pa (2,000 bars). In both systems, when fuel is pressurized, the fuel often heats up to temperatures of around 100 ° C or more.
[007] In common tube injection systems, fuel is stored at high pressure in the central accumulator tube or in separate accumulators before being delivered to the injectors. Often, some of the heated fuel goes back to the low pressure side of the fuel system or back to the fuel tank. In pump and nozzle injection systems, fuel is compressed inside the injector to generate high injection pressures. This, in turn, increases the temperature of the fuel.
[008] In both systems, fuel is present in the injector body before injection where it is additionally heated due to the heat coming from the combustion chamber. The fuel temperature at the tip of the injector can be as high as 250 to 350 ° C.
[009] In this way, the fuel is subjected to pressures of 1.35 x 108 Pa (1,350 bars) to more than 2 x 108 Pa (2,000 bars) and temperatures of about 100 ° C to 350 ° C before injection, it is sometimes recirculated back to the fuel system, thereby increasing the time the fuel experiences these conditions.
[0010] A common problem with diesel engines is the blockage of the injector, particularly the injector body, and the injector nozzle. Clogging can also occur in the fuel filter. Blockage of the injector nozzle occurs when the nozzle is blocked with deposits of diesel fuel. The clogging of fuel filters may be related to the recirculation of fuel back into the fuel tank. Deposits increase with fuel degradation. The deposits can take the form of residues similar to carbonaceous coke or residues similar to gum or sticky. Diesel fuels become more and more unstable the more they are heated, particularly if heated under pressure. In this way, diesel engines that have high pressure fuel systems can cause increased fuel degradation.
[0011] The injector clogging problem can occur when using any type of diesel fuel. However, some fuels can be particularly prone to fouling or clogging can occur more quickly when these fuels are used. For example, it was found that fuels containing biodiesel produce clogging of the injector more quickly. Diesel fuels containing metallic species can also lead to increased deposits. Metal species can be deliberately added to a fuel in additive compositions or they can be present as a contaminating species. Contamination occurs if metal species from fuel distribution systems, vehicle distribution systems, vehicle fuel systems, other metal components and lubricating oils are dissolved or dispersed in the fuel.
[0012] In particular, transition metals cause increased deposits, especially copper and zinc species. These can typically be present in levels of a few ppb (parts per billion) up to 50 ppm, but it is believed that the levels that are likely to cause problems are in the range of 0.1 to 50 ppm, for example, 0.1 to 10 ppm.
[0013] When the injectors are blocked or partially blocked, the delivery of fuel is less efficient and there is an unsatisfactory mixture of the fuel with the air. Over time, this leads to a loss of engine power, increased exhaust emissions and poor fuel economy.
[0014] As the size of the nozzle orifice is reduced, the relative impact of deposit accumulation becomes more significant. Through simple arithmetic, a layer of 5 μm deposit in one orifice and 500 μm reduces the flow area by 4% while the same layer of 5 μm deposit in a 200 μm hole reduces the flow area by 9, 8%.
[0015] Currently, detergents containing nitrogen can be added to diesel fuel in order to reduce the formation of coke. Typical nitrogen-containing detergents are those formed by reacting a polyisobutylene succinic acid derivative substituted with a polyalkylene polyamine. However, newer engines that include thinner nozzles are more sensitive and today's diesel fuels may not be suitable for use with new engines that incorporate these smaller nozzle orifices.
[0016] The present inventor has developed diesel fuel compositions which, when used in diesel engines that have high pressure fuel systems, provide improved performance compared to prior art diesel fuel compositions.
[0017] It is advantageous to provide a diesel fuel composition that prevents or reduces the occurrence of deposits in a diesel engine. Such fuel compositions can be considered to perform a "clean maintenance" function, that is, these compositions prevent or inhibit obstructions.
[0018] However, it would be desirable to provide a diesel fuel composition that helps in cleaning deposits that have already formed in an engine, in particular, deposits that have formed in injectors. Such a fuel composition that, when subjected to combustion in a diesel engine, removes its deposits, thus effecting the "cleaning" of an engine that already contains obstructions.
[0019] Like the "cleaning maintenance" properties, the "cleaning" of an engine with obstructions can provide significant advantages. For example, superior cleaning can lead to an increase in power and / or an increase in fuel economy. In addition, removing deposits from an engine, in particular injectors, can lead to an increase in downtime before maintenance or injector replacement is required, thereby reducing maintenance costs.
[0020] Although, for the reasons mentioned above, injector deposits are a particular problem found in modern diesel engines with high pressure fuel systems, it is desirable to provide a diesel fuel composition that also provides effective detergency in traditional diesel engines older ones so that a single fuel fueled at the pumps can be used in engines of all types.
[0021] It is also desirable that fuel compositions reduce the clogging of vehicle fuel filters. It would be useful to provide compositions that prevent or inhibit the occurrence of fuel filter deposits, that is, to provide a “clean maintenance” function. It would be useful to provide compositions that remove existing deposits from fuel filter deposits, that is, to provide a "clean maintenance" function. Compositions that have the capacity to provide both functions would be especially useful.
[0022] According to a first aspect of the present invention, a diesel fuel composition is provided comprising a first additive (i), comprising a quaternary ammonium salt and a second additive (ii) which comprises a Mannich reaction product; wherein the quaternary ammonium salt additive (i) is formed by the reaction of a compound of formula (A):

[0023] and a compound formed by the reaction of an acylating agent with substituted hydrocarbyl and an amine of formula (B1) or (B2):

[0024] Where R is an optionally substituted alkyl, alkenyl, aryl or alkylaryl group: where R2 and R3 are the same groups or different groups of alkyl, alkenyl or aryl having from 1 to 22 carbon atoms; X is an alkylene bond or group having from 1 to 20 carbon atoms; n is 0 to 20; m is 1 to 5; and R4 is hydrogen or a C1 to C22 alkyl group; and wherein the Mannich reaction product additive (ii) is the product of a Mannich reaction between: (a) an aldehyde; (b) an amine; and (c) a substituted phenol; wherein the phenol is replaced by at least one branched hydrocarbyl group having a molecular weight between 200 and 3,000.
[0025] The additive compounds (i) can be called, in this document, "quaternary ammonium salt additives" or additive (i).
[0026] The additive compounds (ii) can be called, in this document, “Mannich additives” or additive (ii).
[0027] The compound of formula (A), used to prepare the additive (i), is an ester of a carboxylic acid capable of reacting with a tertiary amine to form a quaternary ammonium salt.
[0028] Appropriate compounds of formula (A) include esters of carboxylic acids that have a pKa of 3.5 or less.
[0029] The compound of formula (A) is preferably an ester of carboxylic acid selected from a substituted aromatic carboxylic acid, a-hydroxycarboxylic acid and a polycarboxylic acid.
[0030] In some preferred embodiments the compound of formula (A) is an ester of a substituted aromatic carboxylic acid and thus R is an aryl group.
Preferably R is a substituted aryl group having 6 to 10 carbon atoms, preferably a naphthyl or phenyl group, more preferably a phenyl group. R is suitably substituted with one or more groups selected from carboalkoxy, nitro, cyano, hydroxy, SR5 or NR5R6. Each of R5 and R6 can be optionally substituted hydrogen or carboalkoxy, aryl, alkenyl or alkyl groups. Preferably each of R5 and R6 is hydrogen or an optionally substituted C1 to C22 alkyl group, preferably hydrogen or a C1 to C15 alkyl group, preferably hydrogen or a C1 to C10 alkyl group, more preferably hydrogen or a C1 to C4 alkyl group. Preferably R5 is hydrogen and R6 is hydrogen or a c1 to c4 alkyl group. More preferably, R5 and R6 are hydrogens. Preferably, R is an aryl group substituted by one or more groups selected from hydroxyl, carboalkoxy, nitro, cyano and NH2. R can be a polysubstituted aryl group, for example, trihydroxyphenyl. Preferably, R is a monosubstituted aryl group. Preferably, R is an orthosubstituted aryl group. Suitably R is replaced by a group selected from OH, NH2, NO2 or COOMe. Preferably, R is replaced by an OH or NH2 group. Suitably R is a hydroxy-substituted aryl group. More preferably, R is a 2-hydroxyphenyl group.
[0032] Preferably R1 is an alkylaryl or alkyl group. R1 can be a C1 to C16 alkyl group, preferably a C1 to C10 alkyl group, suitably a C1 to C8 alkyl group. R1 can be a C1 to C16 alkylaryl group, preferably a C1 to C10 alkyl group, suitably a C1 to C8 alkylaryl group. R1 can be methyl, ethyl, propyl, butyl, pentyl, benzyl, or an isomer thereof. Preferably R1 is benzyl or methyl. Most preferably R1 is methyl.
[0033] An especially preferred compound of formula (A) is methyl sacylate.
[0034] In some embodiments the compound of formula (A) is an ester of an α-hydroxycarboxylic acid. In such modalities the compound of formula (A) has the structure:

[0035] where R7 and R8 are the same or different and each is selected from hydrogen, alkyl, alkenyl, aralkyl, or aryl. Such compounds suitable for use in this document are described in EP 1254889
[0036] Examples of compounds of formula (A) in which RCOO is the residue of a D-hydroxycarboxylic acid include methyl-, ethyl-, propyl-, butyl-, pentyl-, hexyl-, benzyl-, phenyl-, and esters 2-hydroxy-isobutyric acid allyl; methyl-, ethyl-, propyl-, butyl-, pentyl-, hexyl-, benzyl-, phenyl-, and 2-hydroxy-2-methylbutyric acid allyl esters; methyl-, ethyl-, propyl-, butyl-, pentyl-, hexyl-, benzyl-, phenyl-, and 2-hydroxy-2-ethylbutyric acid allyl esters; methyl-, ethyl-, propyl-, butyl-, pentyl-, hexyl-, benzyl-, phenyl- and lactic acid allyl esters; and methyl-, ethyl-, propyl-, butyl-, pentyl-, hexyl-, allyl-, benzyl- and phenyl esters of glycolic acid. Among the aforementioned, a preferred compound is methyl 2-hydroxybutyrate.
[0037] In some embodiments the compound of formula (A) is an ester of a polycarboxylic acid. This definition is intended to include dicarboxylic acids and carboxylic acids that have more than 2 chemical portions of acid. In such embodiments RCOO is preferably present in the form of an ester, which is one or more groups of additional acids present in the group R which are in esterified form. Preferred esters are C1 to C4 alkyl esters.
[0038] Compound (A) can be selected from oxalic acid diester, phthalic acid diester, maleic acid diester, malonic acid diester or citric acid diester. A specifically preferred compound of formula (A) is dimethyl oxalate.
[0039] In preferred embodiments the compound of formula (A) is an ester of a carboxylic acid that has a pKa of less than 3.5. In such embodiments, in which the compound includes more than one acid group, we want to refer to the first dissociation constant.
[0040] Compound (A) can be selected from an ester of a carboxylic acid selected from one or more oxalic acid, phthalic acid, salicylic acid, maleic acid, malonic acid, citric acid, nitrobenzoic acid, aminobenzoic acid and 2 , 4,6-trihydroxybenzoic.
[0041] Preferred compounds of formula (A) include dimethyl oxalate, methyl 2-nitrobenzoate and methyl salicylate.
[0042] To form the quaternary ammonium salt additives of the present invention, the compound of formula (A) reacts with a compound formed by the reaction of an acylating agent with substituted hydrocarbyl and an amine of formula (B1) or (B2) .
[0043] When a compound of formula (B1) is used, R4 is preferably hydrogen or a C1 to C16 alkyl group, preferably a C1 to C10 alkyl group, more preferably a C1 to C6 alkyl group. When R4 is alkyl, it can be straight or branched. R4 can be replaced, for example, with a hydroxy or alkoxy substituent. Preferably, R4 is not a substituted alkyl group. More preferably, R4 is selected from hydrogen, methyl, ethyl, propyl, butyl and isomers thereof. Most predictably, R4 is hydrogen.
[0044] When a compound of formula (B2) is used, m is preferably 2 or 3, more preferably 2; n is preferably 0 to 15, preferably 0 to 10, more preferably 0 to 5. Most preferably n is 0 and the compound of formula (B2) is an alcohol.
[0045] Preferably, the substituted hydrocarbyl acylating agent reacts with a diamine compound of formula (B1).
[0046] R2 and R3 are the same or different alkyl, alkenyl or aryl groups having from 1 to 22 carbon atoms. In some embodiments, R2 and R3 can be joined to form a ring structure, for example, a chemical moiety of piperidine or imidazole. R2 and R3 can be alkyl or branched alkenyl groups. Each can be replaced, for example, with a hydroxy or alkoxy substituent.
Preferably R2 and R3 are each, independently, a C1 to C16 alkyl group, preferably a C1 to C10 alkyl group. R2 and R3 can be, independently, methyl, ethyl, propyl, butyl, pentyl, hexyl, heptyl, octyl or an isomer of any of these. Preferably, R2 and R3 are each independently C1 to C4 alkyl. Predictably, R2 is methyl. Preferably, R3 is methyl.
[0048] X is an alkylene bond or group having from 1 to 20 carbon atoms. In preferred embodiments when X is an alkylene group, that group can be straight or branched. The alkylene group can include a cyclic structure in it. This group can be optionally substituted, for example, by a hydroxy or alkoxy substituent.
[0049] 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. More preferably, X is an ethylene, propylene or butylene group, especially a propylene group.
[0050] 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-1,3-diaminopropane, N, N-dimethyl-1,3-diaminopropane, N, N, N'-trimethylethylenediamine, N, N-dimethyl-N'-ethylethylenediamine, N, N- diethyl-N'-methylethylenediamine, N, N, N'-triethylethylenediamine, 3-dimethylaminopropylamine, 3-diethylaminopropylamine, 3-dibutylaminopropylamine, N, N, N'-trimethyl-1,3-propanediamine, N, N, 2,2 -tetramethyl-1,3-propanediamine, 2-amino-5-diethylaminopentane, N, N, N ', N'-tetraethyldiethylenetriamine, 3,3'-diamino-N-methyldipropylamine, 3,3'-iminobis (N, N -dimethylpropylamine), 1- (3-aminopropyl) imidazole and 4- (3-aminopropyl) morpholine, 1- (2-aminoethyl) piperidine, 3,3-diamino-N-methylldipropylamine, 3,3 -aminobis (N, N-dimethylpropylamine), or combinations thereof.
[0051] In some preferred embodiments, the compound of formula (B1) is selected 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.
[0052] 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-dimethylamino-ethanol, 2- dimethylamino-2-methyl-1-propanol.
[0053] In some preferred embodiments, 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.
[0054] An especially preferred compound of formula (B1) is dimethylaminopropylamine.
[0055] The amine of formula (B1) or (B2) reacts with an acylating agent with substituted hydrocarbyl. The substituted hydrocarbyl acylating agent can be based on a mono-, di- or polycarboxylic acid with substituted hydrocarbyl or a reactive equivalent thereof. Preferably, the substituted hydrocarbyl acylating agent is a succinic acid compound with substituted hydrocarbyl 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 can comprise up to about 200 carbon atoms. Preferably, the hydrocarbyl substituent has a numerical average molecular weight (Mn) between 170 to 2,800, for example, from 250 to 1,500, preferably from 500 to 1,500, more preferably, 500 to 1,100. A 700 to 1,300 Mn is especially preferred.
[0057] Hydrocarbyl-based substituents can be produced from homo- or interpolymers (eg copolymers, terpolymers) of mono- and diolefins having 2 to 10 carbon atoms, eg ethylene, propylene, butane- 1, isobutene, butadiene, isoprene, 1-hexene, 1-octene, etc. Preferably, these olefins are 1-mono-olefins. The hydrocarbyl substituent can also be derived from the halogenated analogs (e.g., chlorinated or brominated) of such homo- or interpolymers. Alternatively, the substituent can be produced from other sources, for example, monomeric high molecular weight alkenes (eg 1-tetra-contene) and chlorinated analogues and hydrochlorinated analogues thereof, aliphatic oil fractions, eg waxes paraffin and cracked and chlorinated analogues and hydrochlorinated analogues thereof, white oils, synthetic alkenes, for example, produced by the Ziegler-Natta process (for example, poly (ethylene) greases) and other sources known to those skilled in the art. Any unsaturation in the substituent can, if desired, be reduced or eliminated by hydrogenation according to procedures known in the art.
[0058] The term "hydrocarbyl" as used in this document denotes a group that has a carbon atom directly attached to the remainder of the molecule and that has a predominantly aliphatic hydrocarbon character. Suitable hydrocarbyl-based groups can contain chemical moieties without hydrocarbon. For example, they can contain up to one hydrocarbyl-free group for every ten carbon atoms as long as that hydrocarbyl-free group does not significantly alter the predominantly hydrocarbon character of the group. Those skilled in the art will be aware of such groups, which include, for example, hydroxyl, oxygen, halo (especially chlorine and fluoro), alkoxy, alkyl mercapto, alkyl sulfoxy, etc. Preferred hydrocarbyl-based substituents have a purely aliphatic hydrocarbon character and do not contain such groups.
[0059] Hydrocarbyl-based substituents are preferably and predominantly saturated, that is, they contain no more than one unsaturated carbon-carbon bond for every ten simple carbon-carbon bonds present. Most preferably, the substituents contain no more than one unsaturated carbon-carbon bond for every 50 carbon-carbon bonds present.
Preferred hydrocarbyl-based substituents are poly (isobutene) known in the art. Thus, in especially preferred embodiments, the substituted hydrocarbyl acylating agent is a succinic anhydride with substituted polyisobutenyl.
[0061] The preparation of succinic anhydrides with substituted polyisobutenyl (PIBSA) is documented in the art. Suitable processes include the thermal reaction of polyisobutenes with maleic anhydride (see, for example, US-A-3,361,673 and US-A-3,018,250) and the reaction of a halogenated polyisobutylene (PIB), in in particular, a chlorinated one, with maleic anhydride (see, for example, US-A-3,172,892). Alternatively, polyisobutenyl succinic anhydride can be prepared by mixing the polyolefin with maleic anhydride and crossing the chlorine through the mixture (see, for example, GB-A-949.981).
[0062] Conventional polyisobutenes and so-called "highly reactive" polyisobutenes are suitable for use in the preparation of additive (i) of the present invention. Highly reactive polyisobutenes are defined, in this context, as polyisobutenes in which at least 50%, preferably 70% or more, of the terminal olefinic double bonds are of the vinylidene type as described in EP 0.565.285. Particularly preferred polyisobutenes are those having more than 80 mol% and up to 100% terminal vinylidene groups such as those described in EP 1,344,785.
[0063] Other preferred hydrocarbyl groups include those having an internal olefin, for example, as described in applicant's published application WO2007 / 015080.
[0064] An internal olefin, as used herein, means any olefin predominantly containing a non-alpha double bond, that is, a beta or higher olefin. Preferably, such materials are, substantially and completely, beta or higher olefins, for example, containing less than 10% by weight of alpha olefin, more preferably, less than 5% by weight or less than 2% by weight. Typical internal olefins include Neodene 1518IO available from Shell.
[0065] Internal olefins are sometimes known as isomerized olefins and can be prepared from alpha olefins through an isomerization process known in the art, or are available from other sources. The fact that they are also known as internal olefins means that they do not necessarily have to be prepared by isomerization.
[0066] Some preferred acylating agents for use in the preparation of the quaternary ammonium salt additives of the present invention are succinic acids or substituted polyisobutene succinic anhydrides. When a compound of formula (B2) reacts with a succinic acylating agent, the resulting product is a succinic ester. When a succinic acylating agent reacts with a compound of formula (B1), where R4 is hydrogen, the resulting product can be a succinimide or a succinamide. When a succinic acylating agent reacts with a compound of formula (B1), in which R4 is not hydrogen, the resulting product is an amide.
[0067] In preferred embodiments, the reaction product of the substituted hydrocarbyl acylating agent and the amine of formula (B1) or (B2) is an imide or an ester.
[0068] In especially preferred embodiments, the quaternary ammonium salt additives of the present invention are tertiary amine salts prepared from dimethylamino propylamine and a substituted polyisobutylene succinic anhydride. The average molecular weight of the polyisobutylene substituent is preferably 700 to 1,300, more preferably 900 to 1,100.
[0069] The 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 imide and then the quaternized with the use of methyl salicylate.
[0070] The quaternary ammonium salt additives of the present invention can be prepared by any suitable methods. Such methods will be known to the person skilled in the art and are exemplified in this document. Typically, quaternary ammonium salt additives will be prepared by heating a compound of formula (A) and a compound prepared by reacting a hydrocarbyl-substituted acylating agent with an amine of formula (B1) or (B2) in a ratio molar ratio of 1: 1, optionally in the presence of a solvent. The resulting crude reaction mixture can be added directly to a diesel fuel, optionally following solvent removal. It was not found that any residual by-products or starting materials, still present in the mixture, cause any detriment to the performance of the additive. Thus, the present invention can provide a diesel fuel composition comprising the reaction product of a compound of formula (A) and a compound formed by the reaction of a hydrocarbyl-substituted acylating agent and an amine of formula (B1) or ( B2).
[0071] The composition of the present invention further comprises a second additive (ii) which is the product of a Mannich reaction between: (a) an aldehyde; (b) an amine; and (c) a substituted phenol; wherein the phenol is replaced by at least one branched hydrocarbyl group having a molecular weight between 200 and 3,000.
[0072] Any aldehyde can be used as an aldehyde component (a) of the Mannich additive. Preferably, the aldehyde component (a) is an aliphatic aldehyde. Preferably, 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.
[0073] The amine component (b) of the Mannich additive can be at least one amino or polyamine compound, which has at least one NH group. Suitable amino compounds include primary or secondary monoamines that have hydrocarbon substituents of 1 to 30 carbon atoms or hydrocarbon substituents with hydroxyl substituted from 1 to about 30 carbon atoms.
[0074] In preferred embodiments, the amine component (b) is a polyamine.
[0075] Polyamines can be selected from any compound including two or more amine groups. Preferably, the polyamine is a (poly) alkylene polyamine (meaning an alkylene polyamine or a polyalkylene polyamine; in each case including a diamine, within the meaning of "polyamine"). Preferably, the polyamine is a (poly) alkylene polyamine in which the alkylene component has 1 to 6, preferably 1 to 4, more preferably 2 to 3 carbon atoms. Most preferably, the polyamine is a (poly) ethylene polyamine (i.e., an ethylene polyamine or a polyethylene polyamine).
[0076] Preferably, the polyamine has 2 to 15 nitrogen atoms, preferably 2 to 10 nitrogen atoms, more preferably, 2 to 8 nitrogen atoms.
[0077] Preferably, the polyamine component (b) includes the chemical portion R1R2NCHR3CHR4NR5R6 wherein each of R1, R2 R3, R4, R5 and R6 is independently selected from hydrogen and an alkyl, alkenyl, alkynyl, aryl, alkylating substituent or optionally substituted arylalkyl.
[0078] Thus, the polyamine reagents used to produce the Mannich reaction products of the present invention preferably include an optionally substituted ethylene diamine residue.
[0079] Preferably, at least one of R1 and R2 is hydrogen. Preferably, both R1 and R2 are hydrogen.
[0080] Preferably, at least two of R1, R2, R5 and R6 are hydrogen.
[0081] Preferably, at least one of R3 and R4 is hydrogen. In some preferred embodiments, each of R3 and R4 is hydrogen. In some embodiments, R3 is hydrogen and R4 is alkyl, for example, C1 to C4 alkyl, especially methyl.
[0082] Preferably, at least one of R5 and R6 is an optionally substituted alkyl, alkenyl, alkynyl, aryl, alkylaryl or arylalkyl substituent.
[0083] In modalities in which at least one of R1, R2, R3, R4, R5 and R6 is not hydrogen, each of these is independently selected from a chemical portion of alkyl, alkenyl, alkynyl, aryl, alkylaryl or arylalkyl optionally replaced. Preferably, each of these is independently selected from hydrogen and an optionally substituted C (1-6) alkyl chemical moiety.
[0084] In particularly preferred compounds, each of R1, R2, R3, R4 and R5 is hydrogen and R6 is an optionally substituted alkyl, alkenyl, alkynyl, aryl, alkylaryl or arylalkyl substituent. Preferably, R6 is an optionally substituted C (1-6) alkyl chemical moiety.
[0085] Such a chemical alkyl moiety may be substituted by one or more groups selected from hydroxyl, amino (especially unsubstituted amino; -NH-, -NH2), sulfo, sulfoxy, C (1-4) alkoxy, nitro , halo (especially chlorine or fluoro) and mercapto.
[0086] There may be one or more heteroatoms incorporated into the alkyl chain, for example, O, N or S, to provide an ether, amine or thioether.
[0087] Especially preferred substituents R1, R2, R3, R4, R5 or R6 are hydroxy-C (1-4) alkyl and amino- (C (1-4) alkyl, especially HO-CH2- CH2- and H2N -CH2-CH2-.
[0088] Suitably, the polyamine includes only the amine functionality, or amine and alcohol functionalities.
[0089] The polyamine can be, for example, selected from ethylenediamine, diethylenetriamine, triethylenetetramine, tetraethylene pentamine, pentaethylene-hexamine, hexaethylene heptamine, heptaethyleneoctamine, propane-1,2-diamine, 2 (2-amino-ethylamine) ethanol and ', N'-bis (2-aminoethyl) ethylenediamine (N (CH2CH2NH2) 3). More preferably, the polyamine comprises tetraethylenepentamine or ethylenediamine.
[0090] Commercially available sources of polyamines typically contain mixtures of isomers and / or oligomers and products prepared from such commercially available mixtures are within the scope of the present invention.
[0091] The polyamines used to form the Mannich additives of the present invention can have straight or branched chains and can include cyclic structures.
[0092] The phenol component (c) used to prepare the Mannich additives of the present invention can be substituted by 1 to 4 groups on the aromatic ring (in addition to the OH phenol). For example, it can be a tri or substituted diphenol. More preferably, component (c) is a substituted monophenol. The substitution can be in the ortho and / or goal position and / or to.
[0093] Each chemical portion of phenol can be ortho, meta or para replaced by the aldehyde / amine residue. The compounds in which the aldehyde residue is ortho or substituted are most commonly formed. Mixtures of compounds may result. In preferred embodiments, the starting phenol is to be substituted and thus results in the ortho substituted product.
[0094] Phenol can be substituted by any common group, for example, one or more of an alkyl group, an alkenyl group, an alkynyl group, a nitrile group, a carboxylic acid, an ester, an ether, an alkoxy group, a halo group, an additional hydroxyl group, a mercapto group, an alkyl mercapto group, an alkyl sulfoxy group, a sulfoxy group, an aryl group, an arylalkyl group, a substituted or unsubstituted amino group or a nitro group.
[0095] As mentioned above, phenol includes at least one branched hydrocarbyl substituent. The hydrocarbyl substituent can be optionally substituted by, for example, hydroxyl, halo, (especially chlorine and fluoro), alkoxy, alkyl, mercapto, alkyl sulfoxy, aryl or amino residues. Preferably, the hydrocarbyl group consists essentially of carbon and hydrogen atoms. The substituted phenol can include an alkenyl or alkynyl residue including one or more double and / or triple bonds.
[0096] Hydrocarbyl-based substituents are preferably predominantly saturated, that is, they contain no more than one unsaturated carbon-carbon bond for every ten simple carbon-carbon bonds present. Most preferably, the substituents contain no more than one unsaturated carbon-carbon bond for every 50 carbon-carbon bonds present.
[0097] Preferably, component (c) is a monoalkyl phenol, especially a para-substituted monoalkyl phenol in which the alkyl chain of the substituent is branched.
[0098] In preferred embodiments, the phenol component (c), used to prepare the Mannich reaction product additive (ii), includes a predominant or completely saturated branched hydrocarbyl substituent. Preferably, that predominant or completely saturated hydrocarbyl substituent is branched along the length of the chain. Branched (a) is understood to be along the length of the chain that there are multiple branches of the main (or longer) chain. Preferably, there is a branch at least every 10 carbon atoms along the main chain, preferably at least every 6 carbons, suitably at least every 4 carbons, for example, every 3 carbon atoms or every 2 carbon atoms.
[0099] A particular carbon atom in the main hydrocarbyl chain (which is preferably an alkylene chain) can have one or two branching hydrocarbyl groups. Branching hydrocarbyl groups are understood to be hydrocarbyl groups that are not part of the main chain, but are directly attached to it. Thus, the main hydrocarbyl chain can include the chemical portion -CHR1- or -CR1R2- where R1 and R2 are branching hydrocarbyl groups.
Preferably, each branching hydrocarbyl group is an alkyl group, preferably a C1 to C4 alkyl group, for example, propyl, ethyl or, more preferably, methyl.
[00101] In some preferred embodiments, the phenol component (c), used to prepare the Mannich reaction product additive (ii), includes a hydrocarbyl substituent that is replaced by methyl groups along its main chain. Suitably, there is a plurality of carbon atoms which each have two methyl substituents.
[00102] Preferably, the branch points are substantially evenly spaced along the main chain of the hydrocarbyl group of the phenol component (c).
[00103] Component (c) used to prepare the additive (ii) includes at least one branched hydrocarbyl substituent. This is preferably an alkyl substituent. In especially preferred embodiments, the hydrocarbyl substituent is derived from a polyalkene, suitably a branched alkene polymer, for example, polyisobutene or polypropene.
[00104] In especially preferred embodiments, component (c) used in the preparation of Mannich reaction product additive (ii) includes a substituent derived from poly (isobutene).
[00105] Thus, the Mannich reaction product additives (ii) used in the present invention preferably include a hydrocarbyl chain that has a repeating unit:

[00106] Poly (isobutenes) are prepared by adding isobutene polymerization, (CH3) 2C = CH2. Each molecule of the resulting polymer will include a single chemical portion of alkene.
[00107] Conventional polyisobutenes and so-called "highly reactive" polyisobutenes are suitable for use in the preparation of the additive (ii) of the present invention. Highly reactive polyisobutenes are defined, in this context, as polyisobutenes in which at least 50%, preferably 70% or more, of the terminal olefinic double bonds are of the vinylidene type, as described in EP 0.565.285. Particularly preferred polyisobutenes are those that have more than 80 mol% and up to 100% terminal vinylidene groups such as those described in EP 1,344,785.
[00108] Methods for preparing substituted phenol polyalkylenes, for example, substituted phenol polyisobutenes are known to the person skilled in the art and include the methods described in EP 831,141.
[00109] The hydrocarbyl substituent of component (c) has an average molecular weight of 200 to 3,000. 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 component's hydrocarbyl substituent (c) has an average molecular weight of at least 375, preferably at least 400, suitably at least 475, for example, at least 500.
[00110] In some embodiments, component (c) may include a hydrocarbyl substituent having an average molecular weight of up to 2,800, preferably up to 2,600, for example, up to 2,500 or up to 2400.
[00111] In some embodiments, the hydrocarbyl substituent of component (c) has an average molecular weight of 400 to 2,500, for example, from 450 to 2,400, preferably from 500 to 1,500, suitably from 550 to 1,300.
[00112] In some embodiments, the hydrocarbyl substituent of component (c) has an average molecular weight of 200 to 600.
[00113] In some embodiments, the hydrocarbyl substituent of component (c) has an average molecular weight of 500 to 1000.
[00114] In some embodiments, the hydrocarbyl substituent of component (c) has an average molecular weight of 700 to 1,300.
[00115] In some embodiments, the hydrocarbyl substituent of component (c) has an average molecular weight of 1,000 to 2,000.
[00116] In some embodiments, the hydrocarbyl substituent of component (c) has an average molecular weight of 1,700 to 2,600, for example, 2,000 to 2,500.
[00117] Unless otherwise stated, all average molecular weights cited in this document are numerical average molecular weights.
[00118] The components (a), (b) and (c) used to prepare Mannich product additives (ii) can each comprise a mixture of compounds and / or a mixture of isomers.
[00119] Mannich's additive is preferably the reaction product obtained by reacting components (a), (b) and (c) in a molar ratio between 5: 1: 5 to 0.1: 1: 0.1, more preferably, from 3: 1: 3 to 0.5: 1: 0.5.
[00120] To form the Mannich additive of the present invention, components (a) and (b) are preferably reacted in a molar ratio between 6: 1 to 1: 4 (aldehyde: amine), preferably from 4: 1 to 1: 2, more preferably 3: 1 to 1: 1.
[00121] In preferred embodiments, the molar ratio between component (a) and 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.
[00122] Preferably, the molar ratio between component (a) and 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.
[00123] Preferably, the molar ratio between component (a) and component (b) (aldehyde: amine) in the reaction mixture used to prepare the Mannich additive of the present invention is 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.
[00124] To form a preferred Mannich additive of the present invention, the molar ratio between component (a) and component (c) (aldehyde: phenol) in the reaction mixture is preferably 5: 1 to 1: 4, preferably, from 3: 1 to 1: 2, for example, from 2: 1 to 1: 1.
[00125] In preferred embodiments, the molar ratio between component (a) and 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.
[00126] Preferably, the molar ratio between component (a) and component (c) (aldehyde: phenol) 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.
[00127] Suitably, the molar ratio between component (a) and component (c) (aldehyde: phenol) in the reaction mixture used to prepare the Mannich additive is 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: more preferably from 1 , 3: 1 to 1.55: 1.
[00128] To form the Mannich additive of the present invention, components (c) and (b) are preferably reacted in a molar ratio between 6: 1 to 1: 4 (phenol: amine), preferably from 4: 1 to 1: 2, more preferably, 3: 1 to 1: 2 and, more preferably, 2: 1 to 1: 2.
[00129] Suitably, the molar ratio between component (c) and component (b) (phenol: amine) in the reaction mixture is 0.7: 1 to 1.9: 1, preferably 0.8: 1 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.
[00130] In preferred embodiments, the molar ratio between component (c) and 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.
[00131] Preferably, the molar ratio between component (c) and 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.
[00132] In some preferred embodiments, in the Mannich reaction used to form the additive, the molar ratio between component (a) and component (b) is 2.2 to 1.01: 1; the molar ratio between component (a) and component (c) is 1.99 to 1.01: 1 and the molar ratio between component (b) and component (c) is 1: 1.01 to 1.99.
[00133] In some preferred embodiments in the reaction used to produce the Mannich additive, the molar ratio between component (a) and component (b) is 2 to 1.6: 1, the molar ratio between component (a ) and component (c) is 1.6 to 1.2: 1 and the molar ratio between component (b) and component (c) is 1: 1.1 to 1.5.
[00134] Some preferred compounds used in the present invention are typically formed by reacting components (a), (b) and (c) in a molar ratio between 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).
[00135] The appropriate treatment rates for the quaternary ammonium salt additive and, when present, Mannich's additive will depend on the desired performance and the type of engine in which the additives are used. For example, different levels of additive may be required to achieve different levels of performance.
[00136] Suitably, the quaternary ammonium salt additive is present in the diesel fuel composition in an amount of 1 to 10,000 ppm, preferably from 1 to 1,000 ppm, more preferably, from 5 to 500 ppm, suitably from 5 to 250 ppm, for example, from 5 to 150 ppm.
[00137] Suitably, the Mannich additive, when used, is present in the diesel fuel composition in an amount of 1 to 10,000 ppm, preferably from 1 to 1,000 ppm, more preferably, from 5 to 500 ppm, suitably from 5 at 250 ppm, for example, from 5 to 150 ppm.
[00138] The ratio of the weight 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.
[00139] As previously established, fuels containing biodiesel or metals are known to cause obstructions. Various fuels, for example, those containing high levels of metals and / or high levels of biodiesel, may require higher treatment rates for the quaternary ammonium salt additive and / or Mannich's additive than fuels that are less critical.
[00140] The diesel fuel composition of the present invention may include one or more additional additives such as those commonly found in diesel fuels. These include, for example, antioxidants, dispersants, detergents, metal deactivating compounds, anti-wax build-up agents, cold flow enhancers, acetane enhancers, turbidity-reducing agents, stabilizers, demulsifiers, antifoam, corrosion inhibitors, lubricity, dyes, markers, combustion enhancers, metal deactivators, odor masks, drag reducers and conductivity enhancers. Examples of suitable amounts of each of these types of additives will be known to the person skilled in the art.
[00141] In some preferred embodiments, the composition further comprises a detergent of the type formed by reacting an acylating agent derived from succinic acid with substituted polyisobutene and a polyethylene polyamine. Suitable compounds are, for example, described in WO2009 / 040583.
[00142] Diesel fuel is any fuel suitable for use in a diesel engine, for use on or off the road. This includes, but is not limited to, fuels described as diesel, marine diesel, heavy fuel oil, industrial fuel oil, etc.
[00143] The diesel fuel composition of the present invention may comprise a petroleum-based fuel oil, especially an intermediate distilled fuel oil. Such distillate fuel oils generally boil within the range of 110 ° C to 500 ° C, for example, 150 ° C to 400 ° C. The diesel fuel can comprise atmospheric distillate or vacuum distillate, cracked gas oil, or a combination in any proportion of refinery and direct distillation streams as thermally distilled and / or catalytically cracked and hydrocracked.
[00144] The diesel fuel composition of the present invention can comprise a Fischer-Tropsch fuel. The composition may comprise non-renewable Fischer-Tropsch fuels such as those described as GTL (gas to liquid), CTL (coal to liquid) and OTL (bituminous sand to liquid) fuels.
[00145] The diesel fuel composition of the present invention can comprise a renewable fuel such as a biofuel composition or a biodiesel composition.
[00146] The diesel fuel composition can comprise 1st generation biodiesel. First generation biodiesel contains esters of, for example, vegetable oils, animal fats and used cooking fats. This form of biodiesel can be obtained through the transesterification of oils, for example, rapeseed oil, soy oil, safflower oil, palm oil 25, corn oil, peanut oil, cottonseed oil, tallow, oil coconut oil, jatropha oil, sunflower seed oil, used cooking oils, hydrogenated vegetable oils or any mixture of these, with an alcohol, usually a mono-alcohol, in the presence of a catalyst.
[00147] The diesel fuel composition can comprise second generation biodiesel. Second generation biodiesel derives from renewable resources such as vegetable oils and animal and processed fats, often at the refinery, often with the use of hydroprocessing, such as the H-Bio process developed by Petrobras. Second generation biodiesel can have quality and properties similar to petroleum based fuel oil streams, for example, renewable diesel produced from vegetable oils, animal fats, etc. and marketed by ConocoPhillips as by Renewable Diesel and Neste as NExBTL.
[00148] The diesel fuel composition of the present invention can comprise third generation biodiesel. Third generation biodiesel uses gasification and Fischer-Tropsch technology, including those described as BTL fuels (biomass for liquid). Third generation biodiesel does not differ widely from some second generation, but it aims to explore the entire plant (biomass) and, thus, expands the base of raw material.
[00149] The diesel fuel composition may contain combinations of any or all of the above diesel fuel compositions.
[00150] In some modalities, diesel fuel comprises a non-renewable Fischer Tropsch fuel and / or biodiesel.
[00151] In some embodiments, the diesel fuel composition of the present invention may be a blended diesel fuel comprising biodiesel. In such combinations, biodiesel can 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%.
[00152] In some embodiments, the diesel fuel composition may comprise a secondary fuel, for example, ethanol. Preferably, however, the diesel fuel composition does not contain ethanol.
[00153] The diesel fuel composition of the present invention may contain a relatively high sulfur content, for example, greater than 0.05% by weight, such as 0.1% or 0.2%.
[00154] However, in preferred embodiments, diesel fuel has a sulfur content of at most 0.05% by weight, more preferably, at most 0.035% by weight, especially at most 0.015%. Fuels with even lower levels of sulfur are also suitable, as are fuels with less than 50 ppm sulfur by weight, preferably less than 20 ppm, for example, 10 ppm or less.
[00155] Commonly, when present, species containing metal will be present as a contaminant, for example, through the corrosion of metal surfaces and metal oxide by acidic species present in the fuel or from lubricating oil. In practice, fuels such as diesel fuels usually come into contact with metal surfaces, for example, in vehicle fueling systems, fuel tanks, means of transporting fuel, etc. Typically, metal-containing contamination may comprise transition metals such as zinc, iron and copper; group I or group II metals as sodium; and other metals like lead.
[00156] In addition to the metal-containing contamination that may be present in diesel fuels, there are circumstances in which metal-containing species may be deliberately added to the fuel. For example, as is known in the art, the type of catalyst carried by metal-containing fuel can be added to aid in the regeneration of trapped particulates. Such catalysts are often based on metals such as iron, cerium, Group I and Group II metals, for example, calcium and strontium, as mixtures or alone. Platinum and manganese are also used. The presence of such catalysts can also give rise to injector deposits when fuels are used in diesel engines that have high pressure fuel systems.
[00157] The contamination containing metal, depending on its source, can be in the form of insoluble particles or soluble compounds or complexes. Fuel-borne catalysts containing metal are often soluble compounds or complexes or colloidal species.
[00158] In some embodiments, metal-containing species comprise a fuel-borne catalyst.
[00159] In some embodiments, metal-containing species comprise zinc.
[00160] In a preferred embodiment, the diesel fuel composition of the invention comprises a fuel-borne catalyst that 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.
[00161] Typically, the number of species containing metal in the diesel fuel, expressed in terms of the total weight of metal in the species, 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.
[00162] The fuel compositions of the present invention show improved performance when used in diesel engines that have high pressure fuel systems compared to prior art diesel fuels.
[00163] According to a second aspect of the present invention, an additive package is provided which, upon addition to a diesel fuel, provides a composition of the first aspect.
[00164] The additive package may comprise a mixture of the quaternary ammonium salt additive, the Mannich additive and, optionally, additional additives, for example, those described above. Alternatively, the additive package may comprise an additive solution, suitably in a mixture of hydrocarbon solvents, for example, aliphatic and / or aromatic solvents; and / or oxygenated solvents, for example, alcohols and / or ethers.
[00165] According to a third aspect of the present invention, a method of operating a diesel engine is provided, wherein the method comprises combustion in the engine of a composition of the first aspect.
[00166] In accordance with a fourth aspect of the present invention, the use of a quaternary ammonium salt additive (i) and a Mannich reaction product additive (ii) in a diesel fuel composition is provided to enhance the engine performance of a diesel engine when using said diesel fuel composition.
[00167] The preferred characteristics of the second, third and fourth aspects are as defined in relation to the first aspect.
[00168] Performance improvement can be achieved by reducing or preventing the formation of deposits in a diesel engine. This can be seen as an improvement in “clean maintenance” performance. Accordingly, the present invention can provide a method of reducing or preventing the formation of deposits in a diesel engine by combustion of a composition of the first aspect in said engine.
[00169] Performance improvement can be achieved by removing existing deposits on a diesel engine. This can be seen as an improvement in “cleaning” performance. Accordingly, the present invention can provide a method of removing deposits from a diesel engine by combustion of a composition of the first aspect in said engine.
[00170] In especially preferred embodiments, the composition of the first aspect of the present invention can be used to provide an improvement in "cleaning maintenance" and "cleaning" performance.
[00171] In some preferred embodiments, the use of the third aspect may be related to the use of 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, in which the diesel engine has a high pressure fuel system.
[00172] Modern diesel engines that have a high pressure fuel system can be characterized in a number of ways. Such engines are typically equipped with fuel injectors that have a plurality of openings, each opening having an inlet and an outlet.
[00173] Such modern diesel engines can be characterized by openings that are tapered so that the inlet diameter of the spray holes is larger than the outlet diameter.
[00174] Such modern motors can be characterized by openings having an outlet diameter less than 500 μm, preferably less than 200 μm, more preferably less than 150 μm, preferably less than 100 μm, more preferably less than 80 μm or less.
[00175] Such modern diesel engines can be characterized by openings in which an inner edge of the inlet is rounded.
[00176] Such modern diesel engines can be characterized by the injector that has more than one opening, suitably, more than 2 openings, preferably more than 4 openings, for example, 6 or more openings.
[00177] Such modern diesel engines can be characterized by a peak operating temperature in excess of 250 ° C.
[00178] Such modern diesel engines can be characterized by a fuel pressure greater than 135 MPa (1,350 bar), preferably greater than 150 MPa (1,500 bar), more preferably, greater than 200 MPa (2,000 bar) ).
[00179] The use of the present invention preferably improves the performance of an engine that has one or more of the characteristics described above.
[00180] The present invention is particularly useful in preventing or reducing or removing deposits in engine injectors that operate at high pressures and temperatures, in which the fuel can be recirculated and which comprise a plurality of fine openings 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 that incorporate a high-speed direct injection engine (or HSDI) can, for example, benefit from the present invention.
[00181] Inside the injector body of modern diesel engines, which have a high pressure fuel system, there can be clearances of only 1 to 2 μm between the moving parts and there are reports of engine problems in the field caused by gluing injectors and particularly bonding of open injectors. Deposit control in this area can be very important.
[00182] The diesel fuel compositions of the present invention can also provide improved performance when used with traditional diesel engines. Preferably, improved performance is achieved when using diesel fuel compositions in modern diesel engines that have high pressure fuel systems and when using compositions in traditional diesel engines. This is important due to the fact that it allows a single fuel to be supplied that can be used in new engines and older vehicles.
[00183] The performance improvement of the diesel engine system can be measured in numerous ways. The appropriate methods will depend on the type of engine and whether "cleaning maintenance" and / or "cleaning" performance is measured.
[00184] One of the ways in which performance improvement can be measured is by measuring the power loss in a controlled engine test. An improvement in “clean maintenance” performance can be measured by observing a reduction in power loss compared to what was seen in a base fuel. The "cleaning" performance can be observed by increasing the power when the diesel fuel compositions of the invention are used in an engine with already obstructions.
[00185] The performance improvement of the diesel engine that has a high pressure fuel system can be measured by an improvement in fuel economy.
[00186] The use of the third aspect can also improve the performance of the engine by reducing, avoiding or removing deposits on the vehicle fuel filter.
[00187] The level of deposits in a vehicle fuel filter can be measured quantitatively or qualitatively. In some cases, this can be determined only by inspecting the filter once the filter has been removed. In other cases, the level of deposits can be estimated during use.
[00188] Many vehicles are equipped with a fuel filter that can be visually inspected during use to determine the level of accumulation of solids and the need to change the filter. For example, such a system uses a filter reservoir inside a transparent housing allowing the filter, the level of fuel inside the filter and the degree of filter blockage to be observed.
[00189] The use of the fuel compositions of the present invention can result in levels of deposits on the fuel filter that are considerably reduced compared to the different fuel compositions of the present invention. This allows the filter to be changed less frequently and can ensure that the fuel filters do not fail between service intervals. Thus, the use of the compositions of the present invention can lead to reduced maintenance costs.
[00190] In some embodiments, the occurrence of deposits on a fuel filter can be inhibited or reduced. In this way, a performance of "maintenance of cleanliness" can be observed. In some embodiments, existing tanks can be removed from a fuel filter. In this way, a "cleaning" performance can be observed.
[00191] The performance improvement can also be analyzed considering the extent to which the use of the fuel compositions of the invention reduces the amount of deposit in the injector of an engine. For the “cleaning maintenance” performance, a reduction in the occurrence of deposits would be observed. For the “cleaning” performance, a removal of existing deposits would be observed.
[00192] The direct measurement of accumulated deposit is not usually disregarded, but it is usually deduced from the loss of power or fuel flow rates through the injector.
[00193] The use of the third aspect can improve the performance of the engine by reducing, avoiding or removing deposits, including gums and lacquers inside the injector body.
[00194] In Europe, the European Coordination Council for the development of performance tests for the transportation of fuels, lubricants and other fluids (the industrial body known as CEC) has developed a new test, called CEC F-98-08, to analyze whether diesel fuel is suitable for use in engines according to the new European Union emission standards known as the “Euro 5” standards. The test is based on a Peugeot DW10 engine using Euro 5 injectors and will henceforth be called the DW10 test. This will be further described in the context of the examples (see example 7).
[00195] Preferably, the use of the fuel composition of the present invention promotes reduced deposits in the DW10 test. For “clean maintenance” performance, a reduction in the occurrence of deposits is preferably observed. For “cleaning” performance, deposit removal is preferably observed. The DW10 test is used to measure power loss in modern diesel engines that have a high pressure fuel system.
[00196] For older engines, an improvement in performance can be measured using the XUD9 test. This test is described in relation to example 10.
[00197] Suitably, the use of a fuel composition of the present invention can provide "cleanliness maintenance" performance in modern diesel engines, that is, the formation of deposits on the injectors of these engines can be inhibited or prevented. Preferably, this performance occurs so that a power loss of less than 5% is observed, preferably less than 2% after 32 hours as measured by the DW10 test.
[00198] Suitably, the use of a fuel composition of the present invention can provide a "clean" performance in modern diesel engines, that is, the deposits on the injectors of an engine with already obstructions can be removed. Preferably, this performance occurs so that the power of an engine with obstructions can return to 1% of the level reached with the use of clean injectors within 32 hours as measured in the DW10 test.
[00199] Preferably, rapid "cleaning" can be achieved since the power returns to 1% of the level observed with the use of clean injectors in 10 hours, preferably in 8 hours, suitably in 6 hours, preferably in 4 hours, more preferably, in 2 hours.
[00200] Clean injectors can include new injectors or injectors that have been removed and physically subjected to cleaning, for example, in an ultrasound bath.
[00201] Suitably, the use of a fuel composition of the present invention can provide "cleanliness maintenance" performance in traditional diesel engines, that is, the formation of deposits on the injectors of these engines can be inhibited or avoided. Preferably, this performance occurs so that a loss of flow less than 50%, preferably less than 30% is observed after 10 hours, as measured by the XUD-9 test.
[00202] Suitably, the use of a fuel composition of the present invention can provide a "cleaning" performance in traditional diesel engines, that is, deposits in the injectors of an engine with already obstructions can be removed. Preferably, this performance occurs so that the loss of flow of an engine with obstructions can be increased by 10% or more in 10 hours, as measured in the XUD-9 test.
[00203] Any feature of any aspect of the invention can be combined with any other feature, where appropriate.
[00204] The invention will now be further defined with reference to the following non-limiting examples. Example 1
[00205] Additive A, the reaction product of an acylating agent with substituted hydrocarbyl and a compound of the formula (B1) was prepared as follows:
[00206] 523.88 g (0.425 mol) of PIBSA (made from 1,000 MW of GDP and maleic anhydride) and 373.02 g of Caromax 20 were loaded into a 1 liter vessel. The mixtures were stirred and heated, under nitrogen to 50 ° C. 43.69 g (0.425 mol) of dimethylaminopropylamine were added and the mixture heated to 160 ° C for 5 hours, with concomitant removal of water with the use of a Dean-Stark device. Example 2
[00207] Additive B, a quaternary ammonium salt additive of the present invention was prepared as follows:
[00208] 588.24 g (0.266 mol) of Additive A mixed with 40.66 g (0.266 mol) of methyl salicylate under nitrogen. The mixture was stirred and heated at 160 ° C for 16 hours. The product contained 37.4% solvent. The non-volatile material contained 18% of the quaternary ammonium salt as determined by titration. Example 3
[00209] A substituted polyisobutene phenol was prepared as follows:
[00210] The polyisobutene, which has an average molecular weight of 750 (450.3 g, 0.53 mol, 1 equivalent), was heated to 45 to 50 ° C and then the phenol (150.0 g , 1.59 mol, 3 equivalents) was added. The cloudy mixture was stirred and boron trifluoride dieterate (15.0 g, 0.10 mol, 0.18 equivalent) was added in 2 to 3 ml aliquots over approximately two hours to provide a clear orange liquid, which it was stirred at 45 to 50 ° C for 5 hours. Then, 35% aqueous ammonia (10.5 g, 0.22 mol) was added and the reaction mixture stirred for 30 minutes. Vacuum distillation provided 81.3 g of distillate. This was stirred at 70 ° C in toluene (250.3 g) for 5 minutes, before adding 250.4 g of water. The layers were separated and the toluene extract was washed two more times with water. Residual water and toluene were removed in vacuo to provide the product as a pale yellow viscous liquid. (510.9 g) has a toluene content of 2% by weight and a phenol content less than 0.2% by weight. Example 4
[00211] Additive C, a Mannich additive of the present invention was prepared as follows:
[00212] Phenol PIB 750 (a phenol that has a polyisobutenyl substituent of average molecular weight 750) with a residual GDP content of 5% by weight (447.8 g, 425.4 g of "active" PIB phenol , 0.50 mol, 1.3 equivalent) was mixed with ethylenediamine (25.3 g, 0.38 mol, 1 equivalent) and Caromax 20 solvent (225.6 g). The homogeneous mixture was heated from 90 to 95 ° C. Then, 36.7% formalin (57.12 g, 0.69 mol, 1.8 equivalent) was added over one hour and the reaction mixture was then maintained at 95 ° C for 1 hour. The water was removed using a Dean-Stark device. After distillation, 708.3 g of product were collected. Example 5
[00213] Additive D, a quaternary ammonium salt additive of the present invention was prepared as follows:
[00214] 33.9 kg (27.3 moles) of a succinic anhydride with substituted polyisobutyl, which has a molecular weight of 1,000 GDP, were heated to 90 ° C. 2.79 kg (27.3 moles) of dimethylaminopropylamine were added and the mixture stirred at 90 to 100 ° C for 1 hour. The temperature was increased to 140 ° C for 3 hours with concomitant water removal. 25 kg of 2-ethyl hexanol were added, followed by 4.15 kg of methyl salicylate (27.3 moles) and the mixture maintained at 140 ° C for 9.5 hours. Example 6
[00215] Diesel fuel compositions were prepared by adding the specified additives to aliquots taken from a common lot of base fuel RF06 and containing 1 ppm zinc (as zinc neodecanoate).
[00216] Table 1 below shows the specification for base fuel RF06. Table 1

Example 7
[00217] A diesel fuel composition was prepared by adding 107.5 ppm of the raw material obtained in example 4 (additive C) and 107.5 ppm of the raw material obtained in example 5 (additive D) to a base fuel RF06, which meets the specification given in table 1 above (example 6), along with 1 ppm zinc as zinc neodecanoate. This fuel composition was tested according to method CECF-98-08 DW 10.
[00218] The injector block test engine is the PSA DW10BTED4. Briefly, the engine characteristics are: Model: Four cylinders in line, suspended camshaft, turbocharged with EGR Capacity: 1,998 cm3 Combustion chamber: Four valves, piston tank, direct injection guided by wall Power: 100 kW at 4,000 rpm Torque: 320 Nm at 2,000 rpm Injection system: Standard tube with electronically controlled 6-hole piezo injectors. Maximum pressure: 1.6 x 108 Pa (1,600 bars). Owner's model SIEMENS VDO Emission control: Compliant with Euro IV limit values when combined with exhaust gas after-treatment (DPF) system
[00219] The engine was chosen as a model representative of the European high-speed direct injection diesel engine with the capacity to adapt to current and future European emissions requirements. The common tube injection system uses a highly efficient nozzle model with rounded inlet edges and tapered spray holes for optimal hydraulic flow. This type of nozzle, when combined with high fuel pressure, has enabled advances to be made in combustion efficiency, reduced noise and reduced fuel consumption, but sensitive to influences that can disrupt fuel flow, such as deposit formation in fuel orifices. sprinkling. The presence of these deposits causes a significant loss of engine power and increased gross emissions.
[00220] The test is performed with a future injector model representative of the anticipated Euro V injector technology.
[00221] It is considered necessary to establish a reliable injector condition baseline prior to the start of the clog test, so a sixteen hour run schedule for the test injectors is specified using an unobstructed reference fuel .
[00222] Full details of the CEC F-98-08 test method can be obtained from CEC. The cooking cycle is summarized below.
for an expected range, see method CEC CEC-F-98-08 3. Cool to rest in 60 seconds and rest for 10 seconds 4. Soak period of 4 hours
[00223] The standard CEC F-98-08 test method consists of a 32-hour engine operation that corresponds to 4 repetitions of steps 1 to 3 above and 3 repetitions of step 4. That is, total test time of 56 hours excluding heating and cooling.
[00224] In each case, a first 32-hour cycle was performed with the use of new injectors and RF-06 base fuel that has, added to this, 1 ppm of Zn (as neodecanoate). This resulted in a level of power loss due to the injectors being blocked.
[00225] A second 32-hour cycle was then performed as a 'cleaning' phase. The dirty injectors from the first phase were kept in the engine and the fuel changed to base fuel RF-06 which has, added to this, 1 ppm of Zn (as neodecanoate) and the test additives specified above.
[00226] The test result is shown in Figure 1. Example 8:
[00227] Additive E, a quaternary ammonium salt additive of the present invention was prepared as follows:
[00228] 45.68 g (0.0375 mol) of Additive A were mixed with 15 g (0.127 mol) of dimethyl oxalate and 0.95 g of octanoic acid. The mixture was heated at 120 oC for 4 hours. The excess dimethyl oxalate was removed in vacuo. 35.10 g of the product were diluted with 23.51 g of Caromax 20. Example 9:
[00229] Additive F, a quaternary ammonium salt additive of the present invention was prepared as follows:
[00230] 315.9 g (0.247 mol) of a substituted polyisobutyl succinic anhydride, having a molecular weight PIB of 1,000, were mixed with 66.45 g (0.499 mol) of 2- (2-dimethylamineethoxy) ethanol and 104.38 g of Caromax 20. The mixture was heated to 200 oC with the removal of water. The solvent was removed in vacuo. 288.27 g (0.191 mol) of this product were reacted with 58.03 g (0.381 mol) of methyl salicylate at 150 oC over night and then 230.9 g of Caromax 20 were added. Example 10
[00231] The effectiveness of the additives of the present invention, in older types of engines, can be analyzed using a standard industrial test - CEC test method No CEC F-23-A-01.
[00232] This test measures the formation of injector nozzle coke with the use of a Peugeot XUD9 A / L Engine and provides a means for the discrimination between fuels of different injector nozzle coke propensity. The formation of nozzle coke is the result of carbon deposits that form between the injector needle and the needle seat. The deposition of the carbon deposit occurs due to the exposure of the needle and injector seat to combustion gases, potentially causing undesirable variations in engine performance.
[00233] The Peugeot XUD9 A / L engine is a diesel engine with indirect injection of 4 cylinders of 1.9 liters of purged volume, obtained from Peugeot Citroen Motors, specifically for the method CEC PF023.
[00234] The test engine is equipped with clean injectors that use non-flat injector needles. Air flow at various needle lifting positions was measured on a flow device prior to testing. The engine is operated for a period of 10 hours under cyclical conditions.

[00235] The propensity of the fuel to promote deposit formation in the fuel injectors is determined by measuring the air flow from the injector nozzle again at the end of the test and comparing these values to those before the test. The results are expressed in terms of percentage airflow reduction at various needle lifting positions for all nozzles. The average value of the reduction of air flow in the 0.1 mm needle lift of all four nozzles considers the level of coke formation for a given fuel. Example 11
[00236] Additive G, a quaternary ammonium salt additive of the present invention was prepared as follows:
[00237] 33.9 kg (27.3 moles) of a succinic anhydride substituted by polyisobutyl, which has a molecular weight of 1.000 PIB, were heated to 90 ° C. 2.79 kg (27.3 moles) of dimethylaminopropylamine were added and the mixture stirred at 90 to 100 ° C for 1 hour. The temperature was increased to 140 ° C for 3 hours with concomitant water removal. 25 kg of 2-ethyl hexanol were added, followed by 4.15 kg of methyl salicylate (27.3 moles) and the mixture maintained at 140 ° C for 9.5 hours. Example 12
[00238] Additive H, a quaternary ammonium salt additive of the present invention was prepared as follows:
[00239] A polyisobutyl-substituted succinic anhydride that has a molecular weight of GDP of 260 reacted with dimethylaminopropylamine using a method analogous to that described in example 10. 213.33 g (0.525 mol) of this material was added to 79, 82 (0.525 mol) of methyl salicylate and the mixture heated to 140 ° C for 24 hours before adding 177g of 2-ethylhexanol. Example 13
[00240] Additive J, a quaternary ammonium salt additive of the present invention was prepared as follows:
[00241] A reactor was charged with 201.13 g (0.169 mol) of additive A, 69.73 g (0.59 mol) of dimethyl oxalate and 4.0 g of 2-ethyl hexanoic acid. The mixture was heated at 120 ° C for 4 hours. The excess dimethyl oxalate was removed in vacuo and 136.4 g of Caromax 20 were added. Example 14
[00242] Additive K, a quaternary ammonium salt additive of the present invention was prepared as follows:
[00243] 251.48 g (0.192 mol) of a succinic anhydride replaced by polyisobutyl, which has a GDP molecular weight of 1,000 and 151.96 g of toluene, were heated to 80 ° C. 35.22 g (0.393 mol) of N, N-dimethyl-2-ethanolamine was added and the mixture heated to 140 ° C. 4 g of Amberlyst catalyst was added and the mixture reacted overnight before filtration and solvent removal. 230.07 g (0.159 mol) of this material were reacted with 47.89 g (0.317 mol) of methyl salicylate at 142 ° C overnight before the addition of 186.02 g Caromax 20. Example 15
[00244] Additive L, a quaternary ammonium salt additive of the present invention was prepared as follows:
[00245] A succinic anhydride substituted by polyisobutyl, which has a molecular weight of GDP of 1,300, reacted with dimethylaminopropylamine using a method analogous to that described in example 10. 20.88 g (0.0142 mol) of this material were mixed with 2.2 g (0.0144 mol) of methyl salicylate and 15.4 g 2-ethylhexanol. The mixture was heated at 140 ° C for 24 hours. Example 16
[00246] Additive M, a quaternary ammonium salt additive of the present invention was prepared as follows:
[00247] A polyisobutyl-substituted succinic anhydride, which has a molecular weight of GDP of 2,300, reacted with dimethylaminopropylamine using a method analogous to that described in example 10. 23.27 g (0.0094 mol) of this material it was mixed with 1.43 g (0.0094 mol) of methyl salicylate and 16.5 g of 2-ethylhexanol. The mixture was heated at 140 ° C for 24 hours. Example 17
[00248] A polyisobutyl-substituted succinic anhydride, which has a molecular weight of 750 GDP, reacted with dimethylaminopropylamine using a method analogous to that described in example 10. 31.1 g (0.034 mol) of this material was mixed with 5.2 g (0.034 mol) of methyl salicylate and 24.2 g of 2-ethylhexanol. The mixture was heated at 140 ° C for 24 hours. Example 18
[00249] 61.71 g (0.0484 mol) of a succinic anhydride substituted by polyisobutyl, which has a molecular weight of 1,000 GDP, was heated to 74 ° C. 9.032 g (0.0485 mol) of dibutylaminopropylamine was added and the mixture heated to 135 ° C for 3 hours with the removal of water. 7.24 g (0.0476 mol) of methyl salicylate was added and the mixture reacted overnight before adding 51.33 g Caromax 20. Example 19
[00250] 157.0 g (0.122 mol) of a succinic anhydride substituted by polyisobutyl, which has a molecular weight of 1,000 and 2-ethylhexanol (123.3 g), was heated to 140 ° C. Benzyl salicylate (28.0 g, 0.123 mol) was added and the mixture stirred at 140 ° C for 24 hours. Example 20
[00251] 18.0 g (0.0138 mol) of additive A and 2-ethylhexanol (12.0 g) were heated to 140 ° C. Methyl 2-nitrobenzoate (2.51 g, 0.0139 mol) was added and the mixture stirred at 140 ° C for 12 hours.

权利要求:
Claims (14)
[0001]
1. Diesel fuel composition characterized by the fact that it comprises a first additive (i) which comprises a quaternary ammonium salt and a second additive (ii) which comprises a Mannich reaction product; wherein the quaternary ammonium salt additive (i) is formed by the reaction of a compound of formula (A):
[0002]
2. Diesel fuel composition according to claim 1, characterized by the fact that the compound of formula (A) is an ester of carboxylic acid selected from a substituted aromatic carboxylic acid, a-hydroxycarboxylic acid and an acid polycarboxylic.
[0003]
3. Diesel fuel composition according to claim 2, characterized by the fact that the compound of formula (A) is selected from dimethyl oxalate, methyl 2-nitrobenzoate and methyl salicylate.
[0004]
Diesel fuel composition according to any one of claims 1 to 3, characterized in that the substituted hydrocarbyl acylating agent reacts with a diamine compound of formula (B1).
[0005]
Diesel fuel composition according to any one of claims 1 to 4, characterized in that the additive (i) is a tertiary amine salt prepared from dimethylaminopropylamine and a substituted polyisobutylene succinic anhydride.
[0006]
6. Diesel fuel composition according to any one of claims 1 to 5, characterized by the fact that in the Mannich reaction used to form the additive (ii), the molar ratio between component (a) and component (b ) is 2.2 to 1.01: 1; the molar ratio between component (a) and component (c) is 1.99 to 1.01: 1 and the molar ratio between component (b) and component (c) is 1: 1.01 to 1.99.
[0007]
7. Diesel fuel composition according to claim 6, characterized by the fact that in the reaction used to produce the Mannich additive, the molar ratio between component (a) and component (b) is 2 to 1, 4: 1, the molar ratio between component (a) and component (c) is 1.7 to 1.1: 1 and the molar ratio between component (b) and component (c) is 1: 1.1 to 1.7.
[0008]
Diesel fuel composition according to any one of claims 1 to 7, characterized in that the diesel fuel comprises Fischer Tropsch fuel and / or biodiesel.
[0009]
Diesel fuel composition according to any one of claims 1 to 8, characterized in that it additionally comprises a fuel-borne catalyst that includes a metal selected from iron, cerium, group I and group II metals, platinum, manganese and mixtures of these.
[0010]
10. Additive package characterized by the fact that, upon addition to a diesel fuel, it provides a composition as defined in any one of claims 1 to 9.
[0011]
11. Method of operation of a diesel engine, characterized by the fact that it comprises combustion in the engine of a composition as defined in any one of claims 1 to 9.
[0012]
12. Use of the diesel fuel composition as defined in claim 1, comprising a quaternary ammonium salt additive (i) and a Mannich reaction product additive (ii) characterized by the fact that it improves the engine performance of an engine diesel fuel during the use of said diesel fuel composition, in which the improvement in performance is achieved by reducing or preventing deposit formation in the diesel engine, or by removing existing deposits in the diesel engine.
[0013]
13. Use, according to claim 12, characterized by the fact that it provides "cleaning maintenance" and / or "cleaning" performance.
[0014]
14. Use according to claim 12 or 13, characterized by the fact that it improves the performance of a modern diesel engine that has a high pressure fuel system and / or improves the performance of a traditional diesel engine.

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EP2739707B1|2019-09-25|

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CN103958650A|2014-07-30|

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US9932535B2|2018-04-03|

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GB201113390D0|2011-09-21|

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CA2843190A1|2013-02-07|

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BR112014002541A2|2017-03-14|

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EP2739707A1|2014-06-11|

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CA2843190C|2021-12-14|

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MY166864A|2018-07-24|

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KR102005124B1|2019-07-29|

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AU2012291814A1|2014-02-13|

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KR20140063641A|2014-05-27|

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WO2013017884A1|2013-02-07|

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法律状态:
2018-12-11| B06F| Objections, documents and/or translations needed after an examination request according [chapter 6.6 patent gazette]|

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2019-04-30| B06T| Formal requirements before examination [chapter 6.20 patent gazette]|

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2019-08-20| B07A| Application suspended after technical examination (opinion) [chapter 7.1 patent gazette]|

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2020-08-18| B09A| Decision: intention to grant [chapter 9.1 patent gazette]|

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2020-12-01| B16A| Patent or certificate of addition of invention granted [chapter 16.1 patent gazette]|Free format text: PRAZO DE VALIDADE: 20 (VINTE) ANOS CONTADOS A PARTIR DE 02/08/2012, OBSERVADAS AS CONDICOES LEGAIS. |

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申请号 | 申请日 | 专利标题

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GBGB1113390.7A|GB201113390D0|2011-08-03|2011-08-03|Fuel compositions|

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GB1113390.7|2011-08-03|

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PCT/GB2012/051875|WO2013017884A1|2011-08-03|2012-08-02|Fuel compositions|

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