• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
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  • 优先权
    • 专利摘要:
    A fuel additive concentrate for gasoline, a gasoline fuel comprising an additive mixture, a method for reducing wear in an engine and in a fuel delivery system of a gasoline engine, and a method for improving injector performance. The additive concentrate comprises an aromatic solvent and a mixture which contains: (i) N, N-bis (2-hydroxyethyljalkylamide, (ii) 2 - ((2- (bis (2-hydroxyethyl) amino) ethyl) amino) ethyl alkanoate and N- (2- (bis (2-hydroxyethyl) -amino) ethyl) -N- (2-hydroxyethyl) alkylamide, and (iii) fatty acid ester (s) and amide (s) derived from a self-condensation product of diethanolamine containing at least 3 contains amino groups.
    公开号:BE1025932B1
    申请号:E20180159
    申请日:2018-12-26
    公开日:2019-09-19
    发明作者:Michel Nuckols；Charles Shanahan；Scott A Culley；Keihann Yavari；Hecke Lieven Van
    申请人:Afton Chemical Corp；
    IPC主号:
    专利说明:

    FUEL ADDITIVE MIXTURES AND FUELS THAT PROVIDE THIS
    CONTAIN
    RELATED REQUEST:
    This application is related to a co-pending application filed the same day as a result of a joint development between Afton Chemical Corporation of Richmond, Virginia, Oleon NV of Belgium and Oleon SAS of France.
    TECHNICAL FIELD:
    The disclosure is directed to fuel additives for fuel compositions and to fuel compositions containing the additives. In particular, the disclosure relates to a gasoline fuel additive mixture that has improved friction, wear reduction, and injector deposits in fuel compositions and provides increased low temperature stability to a fuel additive concentrate containing the additive mixture. More specifically, the additive blend is a friction modifier and fuel injector cleaner derived from fatty acids and diethanolamine or self-condensation products of diethanolamine made by a process that improves the low temperature compatibility of fuel additive concentrates containing the additive blend.
    BACKGROUND AND SUMMARY:
    Vehicle fuel compositions are continuously being improved to improve various properties of the fuels to support their use in newer, more advanced engines including
    BE2018 / 0159 gasoline engines with direct injection. Accordingly, fuel compositions typically include additives that target certain properties that require improvement. For example, friction modifiers are added to fuel to reduce friction and wear in the fuel supply systems and piston rings of an engine. In addition, special components can be added to fuel to reduce fouling of the injection nozzle, to clean contaminated injectors and to improve the performance of direct injection combustion engines. When such additives are added to the fuel, some of the additives are transferred to the lubricant thin film in the engine piston ring zone, where it can also reduce friction and wear and thus improve fuel consumption. Such fuel additives are introduced into the crankcase during operation of the engine, so that a fuel additive that is also favorable to the engine lubricant is desirable. However, fuel additive concentrates containing friction modifiers made from diethanolamine and certain fatty acids or their corresponding esters may be unstable when stored at low temperatures and the performance of such friction modifiers is often less than desirable. In addition, certain fatty acid-based amine and alkanolamide friction modifiers are waxes or partially solids that are difficult to handle at low ambient temperatures.
    In particular, friction modifiers made from acids and esters derived from saturated or monounsaturated fatty acids such as laurine, myristine, palmitine, and stearic acid are difficult to formulate into additive concentrates that remain liquid and homogeneous at low temperatures. The instability can be exacerbated by the typical detergent additives used in fuel additive concentrates, such as polyisobutene-Mannich additives. Because additive concentrates are the preferred form to mix fuel additive components into the fuel, it is essential that
    BE2018 / 0159 fuel additive concentrates are homogeneous and remain liquid at low temperatures, preferably to about -20 ° C or lower.
    When the additive concentration of the friction modifier is quite high in the concentrate, compatibility agents and / or large amounts of solvent can be added to the additive composition to improve its solubility at low temperatures. Compatibility agents used include low molecular weight alcohols, esters, anhydrides, succinimides, glycol ethers, and alkylated phenols, and mixtures thereof. Alternatively, some producers of additives have included low molecular weight esters in the reaction mixture of fatty acids with the diethanolamine to improve the low temperature stability of the reaction product. Unfortunately, the costs that solvents, compatibility agents, and low molecular weight esters add to additive concentrates can make their use uneconomical.
    Partial esters of fatty acids and polyhydroxy alcohols such as glycerol monooleate (GMO) and fatty amine ethoxylates such as diethoxylated laurylamine are also known fuel additives that reduce friction and wear and can improve fuel consumption. GMO and some fatty amine ethoxylates have poor compatibility in fuel additive concentrates when the concentrates are stored at low temperatures. It is particularly difficult to prepare fuel additive concentrates that contain both GMO and fatty amine diethoxylates that are stable at low temperatures. Although friction modifiers based on GMO and fatty amethoxylate may improve fuel consumption when added to a fuel, GMO and certain fatty amethoxylates may be unstable in additive concentrates or large amounts of solvent and compatibility agents may be required to keep the additive concentrate stable and fluid at low temperatures. Accordingly, GMO, fatty amine ethoxylates, and fatty alcohol amide friction modifiers cannot be added to a fuel composition in a favorable manner to reduce fuel consumption and
    BE2018 / 0159 to improve the wear protection of the fuel supply system, unless they can be formulated in a stable fuel additive concentrate.
    Many other friction modifiers have been tried, but there remains, however, a need for a friction modifier that can be easily formulated into fuel additive concentrates that are stable at low temperatures, i.e., temperatures as low as about -20 ° C. There is also a need for a friction modifier that improves the low temperature compatibility of other fuel additive components in fuel additive concentrates. In addition, there is a need for a friction modifier that improves the friction and wear properties of other fuel additives. In addition, there is a need for a friction modifier that improves fuel consumption, and that provides wear protection to fuel delivery systems, from other characteristics. Fuel compositions for direct fuel injection engines often produce unwanted deposits in the injectors, engine combustion chambers, fuel delivery systems, fuel filters, and inlet valves. Accordingly, improved compositions are desirable that can prevent the build-up of deposits and maintain cleanliness as new during the life of the vehicle. A composition that can clean contaminated fuel injectors, restore performance to the previous as new condition and improve engine performance is desirable and valuable for reducing exhaust emissions from the air. Although there are additives known to be able to reduce the contamination of the injector nozzle and to reduce the deposits of the inlet valves, the cleaning performance and cleaning effect may be insufficient. Moreover, its stability and interaction with other fuel additives can be unsatisfactory. Accordingly, there remains a need for a fuel additive that is cost effective, can be easily incorporated into additive concentrates, and improves multiple characteristics of a fuel.
    In accordance with the disclosure, exemplary embodiments provide a fuel additive concentrate for gasoline, a
    BE2018 / 0159 gasoline fuel containing an additive mixture, a method for reducing wear in an engine and in a fuel delivery system of a gasoline engine, and a method for improving the injector performance. The additive concentrate comprises an aromatic solvent and a mixture containing (i) N, N-bis (2-hydroxyethyl) alkylamide, (ii) 2 - ((2- (bis (2-hydroxyethyl) amino) ethyl) amino) ethyl alkanoate and N- (2- (bis (2-hydroxyethyl) amino) ethyl) -N- (2-hydroxyethyl) alkylamide, and (iii) fatty acid ester (s) and amide (s) derived from a self-condensation product of diethanolamine (DEA) containing at least 3 amino groups . A weight ratio of (i) to (ii) to (iii) in the concentrate ranges from about 8: 2: 0 to about 2: 5: 3. The fuel additive mixture is essentially free of glycerin and remains liquid at a temperature of up to about -20 ° C.
    In one embodiment, a fuel fuel composition is provided for reducing fuel system wear and engine friction, and for improving the cleanliness of the injector. The composition comprises A) gasoline and B) a fuel additive mixture containing a) N, N-bis (2-hydroxyethyl) alkylamide, b) 2 - ((2- (bis (2-hydroxyethyl) amino) ethyl) amino) ethyl alkanoate and N- (2- (bis (2-hydroxyethyl) amino) ethyl) -N- (2-hydroxyethylalkylalkylamide), and c) fatty acid ester (s) and amide (s) derived from a self-condensation product of diethanolamine (DEA) containing at least 3 amino groups wherein the alkyl groups of the amide (s) and ester (s) contain from 8 to 18 carbon atoms. A weight ratio of (a) to (b) to (c) in the fuel additive mixture ranges from about 8: 2: 0 to about 2: 5: 3. The fuel additive mixture is essentially free of glycerol and remains liquid at a temperature of up to about -20 ° C.
    In accordance with another embodiment of the disclosure, there is provided a method for reducing wear and motor friction. The method comprises providing gasoline that contains a wear-reducing additive mixture consisting essentially of: a) N, N-bis (2-hydroxyethyl-ammonium alkyl), b) 2 - ((2- (bis (2-hydroxyethyl) amino) ethyl) amino) ) ethyl alkanoate and N- (2- (bis (2-hydroxyethyl) amino) ethyl) -N- (2
    BE2018 / 0159 hydroxyethyl) alkylamide, and c) fatty acid ester (s) and amide (s) derived from a self-condensation product of diethanolamine (DEA) containing at least 3 amino groups. The additive mixture is substantially free of glycerol and a weight ratio of (a) to (b) to (c) ranges from about 8: 2: 0 to about 2: 5: 3. The additive mixture is combined with gasoline to provide a fuel composition and the engine is operated on the fuel composition.
    A further embodiment of the disclosure provides a method for improving the injector performance of a fuel-injected gasoline engine. The method comprises providing gasoline containing an injector cleaning additive mixture which essentially contains: a) N, N-bis (2-hydroxyethyl) alkylamide, b) 2 - ((2- (bis (2-hydroxyethyl) amino) ethyl) amino) ) ethyl alkanoate and N- (2- (bis (2-hydroxyethyl) amino) ethyl) -N- (2-hydroxyethyljalkylamide) and c) fatty acid ester (s) and amide (s) derived from a self-condensing product of diethanolamine (DEA) containing at least 3 contains amino groups. The additive mixture is substantially free of glycerol and a weight ratio of (a) to (b) to (c) ranges from about 8: 2: 0 to about 2: 5: 3. The additive mixture is combined with gasoline to provide a fuel composition and the engine is operated on the fuel composition.
    In some embodiments, the additive mixture contains less than 3% by weight of diesters and diamides derived from the reaction of a second fatty acid with the aforementioned alkanolamides and esters and amides and esters derived from self-condensing products from DEA.
    In some embodiments, the additive mixture contains less than 3% by weight of N, N'-bis (2-hydroxyethyl) piperazine, such as less than 0.5% by weight of N, N'bis (2-hydroxyethyl) piperazine based on a total weight of the additive mixture.
    In some embodiments, the additive mixture contains from about 5 to about 30% by weight of fatty acid ester (s) and amide (s) derived from a
    BE2018 / 0159 self-condensing product from DEA containing at least 3 amino groups based on a total weight of the additive mixture.
    In other embodiments, the alkyl groups of the amide (s) and ester (s) contain from 8 to 18 carbon atoms. In some embodiments, 45 to 55% by weight of the alkyl groups in the amide (s) and ester (s) is dodecyl groups. In some embodiments, an additive concentrate for gasoline contains from about 10 to about 90% by weight of the fuel additive mixture described above based on the total weight of the additive concentrate.
    In other embodiments, the fuel additive concentrate also contains one or more detergents and one or more carrier fluids.
    In some embodiments, the fuel additive concentrate further comprises a friction modifier selected from partial esters of fatty acid and polyhydroxy alcohols, N, N-bis (2-hydroxyalkyl) alkylamines, and mixtures thereof, wherein a weight ratio of friction modifier to fuel additive mixture in the concentrate ranges from about 10: 1 to about 1:10 In some embodiments, a gasoline containing the fuel additive mixture described above has a high frequency reciprocating rig (HFRR) wear scar of no more than about 690 µm.
    In some embodiments, a gasoline containing the fuel additive mixture described above has an injector cleaning improvement of 98%.
    In a further embodiment, the fuel composition contains from about 10 to about 1500 ppm by weight, such as from about 40 to about 750 ppm by weight, or from about 50 to about 500 ppm by weight, or from about 50 to about 300 ppm by weight of the fuel additive mixture.
    As explained above, the additive mixture as described herein is, surprisingly and fairly unexpectedly, a stable
    BE2018 / 0159 fuel additive mixture that remains liquid at low temperature and also provides an improvement in friction and wear reduction of a fuel composition containing the additive mixture. It was also surprising and rather unexpected that the additive mixture as described herein was effective in cleaning contaminated fuel injectors, sufficient to provide improved engine performance. The additive mixture also provides a suitable friction and wear reduction that is at least as good, if not better, than the friction and wear reduction provided by conventional friction modifiers.
    Additional embodiments and advantages of the disclosure will be set forth in part in the detailed description that follows and / or may be learned by practicing the disclosure. It is to be understood that both the foregoing general description and the following detailed description serve only as an example and explanation and do not limit the disclosure as claimed.
    DETAILED DESCRIPTION OF EXAMPLE EMBODIMENTS The fuel additive mixture of the present disclosure can be used in a small amount in a large amount of fuel and can be added directly to the fuel or added to the fuel as a component of an additive concentrate.
    As used herein, the term hydrocarbyl group or hydrocarbyl is used in its usual meaning, which is well known to those skilled in the art. In particular, it refers to a group with a carbon atom that is directly attached to the rest of a molecule and with a predominantly hydrocarbon character. Examples of hydrocarbyl groups include:
    (1) hydrocarbon substituents, i.e. aliphatic (e.g., alkyl or alkenyl), alicyclic (e.g., cycloalkyl, cycloalkenyl) substituents, and aromatic, aliphatic and alicyclic substituted aromatic substituents, as well as cyclic substituents in which the ring is completed
    BE2018 / 0159 by another part of the molecule (e.g., two Substituents together form an alicyclic group);
    (2) substituted hydrocarbon substituents, ie Substituents containing non-hydrocarbon groups which, in the context of the disclosure herein, the predominantly hydrocarbon substituent (e.g., halogen (especially chlorine and fluorine), hydroxy, alkoxy, mercapto, alkyl mercapto, nitro, nitroso, amino, alkylamino and sulfoxy);
    (3) hetero-substituents, i.e. Substituents which, although having a predominantly hydrocarbon character, contain, in the context of this disclosure, other than carbon in a ring or chain that is otherwise composed of carbon atoms. Hetero atoms include sulfur, oxygen, nitrogen, and include substituents such as pyridyl, furyl, thienyl, and imidazolyl. In general, no more than two, or as a further example, no more than one, non-hydrocarbon substituent will be present for every ten carbon atoms in the hydrocarbyl group; in some embodiments there will be no non-hydrocarbon substituent in the hydrocarbyl group.
    As used herein, the term large amount means an amount greater than or equal to 50% by weight, relative to the total weight of the composition. In addition, as used herein, the term small amount is understood to mean an amount of less than 50% by weight relative to the total weight of the composition.
    A suitable fuel additive mixture may contain reaction products of a fatty acid, fatty acid ester or mixtures thereof and dialkanolamine or self-condensation products of a dialkanolamine, wherein the alkyl group has from 2 to 4 carbon atoms. The fuel additive mixture is essentially free of glycerol. The N, N-bis (2-hydroxyethyl) alkylamides typically have short chain (C 2 -C 4) hydroxyalkyl groups and a long chain (C 8 -C 24) alkyl group. A suitable compound of this type is derived from coconut oil containing lauric acid as a main component and diethanolamine (DEA). One component of the products used as an effective friction-reducing and injector cleaner in fuel can have the following structure (I):
    BE2018 / 0159
    OH

    wherein R is a hydrocarbyl group having from 8 to 24 carbon atoms, such as from about 10 to 20 carbon atoms or from 12 to 18 carbon atoms, wherein R is linear or branched and may be saturated or unsaturated. A suitable N, N-bis (2-hydroxyalkyl) alkylamide is N, N-bis (2-hydroxyethyl) dodecylamide which is usually derived from coconut fatty acid, so that the R 1 substituent generally ranges from C 5 to C 18, with C 12 and C 14 groups that predominate and are usually straightforward.
    The reaction product suitably contains as a main component or a secondary component a mixture of N, N-bis (2-hydroxyethyl) alkylamides. A small amount of esters may be present after the reaction of a fatty acid, fatty acid ester or mixtures thereof and diethanolamine.
    The reaction product also contains as a component a mixture of amides and esters derived from the reaction of fatty acid with a self-condensation product of diethanolamine. One of the components present in an amount up to about 45% by weight of such products is N- (2- (bis (2-hydroxyethyl) amino) ethyl) -N- (2-hydroxyethyl) alkylamide which has the following structure ( II) has:
    BE2018 / 0159

    wherein R has the same meaning as described above. The formation of product II can arise from the condensation of two diethanolamines. The amine group of one diethanolamine can combine with the hydroxyl group of a second diethanolamine to eliminate water and form a new carbon nitrogen bond, resulting in the formation of N, N, N'-tris (2-hydroxyethyl) ethylenediamine, also referred to as DEA dimer. Tris (2-hydroxyethyl) ethylenediamine then condenses with a fatty acid to form product II. Alternatively, reaction product II may arise from the condensation of DEA with one of the hydroxyl groups of product I and the elimination of water. Also included in products used as effective friction and wear-reducing and injector cleaning agents are amides that result from the self-condensation of three or more diethanolamines, also referred to as DEA trimers. Esters can also be formed by the reaction of a fatty acid, fatty acid ester or mixtures thereof and the self-condensing products of DEA trimers. Although the products used as effective friction and wear-reducing and injector cleaning agents containing two or more nitrogen substances may be the result of two slightly different paths, for clarity these products will be named as arising from DEA dimers, trimers and oligomers.
    Accordingly, the fuel additive mixture comprises at least one fatty acid amide from DEA and at least one fatty acid ester and / or amide
    BE2018 / 0159 of a self-condensing product from DEA, where DEA is a compound of formula (III)
    and wherein the self-condensation products of DEA contain two or more amino groups and can be selected from the DEA dimer, N, N, N'-tris (2-hydroxyethyl) ethylenediamine of formula (IV)
    and the DEA trimers, tetrakis (2-hydroxyethyl) diethylene triamines of the formulas (V) and (VI)
    BE2018 / 0159
    and other DEA self-condensing products, also called DEA oligomers of the formula
    N x (CH 2 CH 2 ) x .i (CH 2 CH 2 OH) x + i (VII) wherein x is an integer from 1 to 6.
    The fatty acid amide of DEA can be derived from a fatty acid or a mixture of fatty acids with from 8 to 18 carbon atoms. In one embodiment, the fatty acid amide of DEA is N, N-bis (210 hydroxyethyl) dodecanamide of formula (VIII)
    The fatty acid amide (s) and ester (s) derived from the self-condensing products of DEA can also have alkyl groups derived from a fatty acid or a mixture of fatty acids with from 8 to 18 carbon atoms. In one embodiment, the fatty acid ester is derived from the self-condensation product of DEA 2 - ((2- (bis (2-hydroxyethyl) amino) ethyl) amino) ethyl dodecanoate of formula (IX):
    BE2018 / 0159 o
    H
    N.
    .OH
    O '(IX) and the fatty acid amide derived from the self-condensation product of DEA is N- (2 (bis (2-hydroxyethyl) amino) ethyl N- (2-hydroxyethyl) dodecanamide of formula (X):
    (X).
    The fatty acid ester and / or amide of the self-condensing product of DEA may also include amide (s) and ester (s) of the self-condensing products of formulas (V), (VI) and (VII).
    In some embodiments, the amount of fatty acid amide (s) derived from DEA of formula (III) can vary from about 20 to about 80% by weight based on the total weight of the additive blend, such as from about 30 to about 75% by weight. %, and suitably from about 40 to about 60% by weight based on the total weight of the additive blend.
    In one embodiment, the additive blend comprises from about 20 to about 30 weight percent N, N-bis (2-hydroxyethyl) dodecanamide, relative to the total weight of the additive blend.
    In other embodiments, the total amount of fatty acid ester (s) and / or amide (s) derived from DEA of formulas (IV), (V), (VI) and (VII) in
    BE2018 / 0159 the additive mixture may vary from about 20 to about 80% by weight of the total weight of the additive mixture, preferably from about 30 to about 60% by weight relative to the total weight of the additive mixture.
    In some embodiments, the amount of fatty acid ester (s) and fatty acid amide (s) of tris (2-hydroxyethyl) ethylenediamine of formula (IV) can range from about 15 to about 60% by weight based on a total weight of the additive mixture such as from about 20 to about 55% by weight of the total weight of the additive mixture, and suitably from about 30 to about 45% by weight of the additive mixture.
    In some embodiments, the amount of fatty acid ester (s) and fatty acid amide (s) derived from DEA self-condensation products other than from tris (2-hydroxyethyl) ethylenediamine of formula (IV) can range from about 5% to about 30% by weight. % of the total weight of the additive mixture, such as from about 10 to about 25% by weight of the total weight of the additive mixture and suitably from about 15 to about 20% by weight of the additive mixture.
    In other embodiments, the additive mixture contains less than 3 wt% (N, N'-bis (2-hydroxyethyl) piperazine (BHEP), such as less than 2 wt% BHEP, or less than 0.5 wt% BHEP and suitably less than 0.2 wt% BHEP based on the total weight of the additive mixture.
    In some embodiments, the additive mixture comprises 40 to about 60% by weight of N, N-bis (2-hydroxyethyl) alkylamide based on the total weight of the additive mixture, from about 30 to about 45% by weight of 2 ((2- (bis (2-hydroxyethyl) amino) ethyl) amino) ethyl alkanoate and N- (2- (bis (2-hydroxyethyl) amino) ethyl) -N- (2-hydroxyethyl) alkylamide based on a total weight of the additive mixture and from about 10% to about 25% by weight of fatty acid ester (s) and amide (s) derived from diethanolamine self-condensing products (DEA) comprising at least 3 amino groups based on the total weight of the mixture.
    In one embodiment, the additive mixture comprises from about 25 to about 40% by weight of N, N-bis (2-hydroxyethyl) dodecanamide based on a
    BE2018 / 0159 total weight of the additive mixture, from about 15 to about 25% by weight of 2 ((2- (bis (2-hydroxyethyl) amino) ethyl) amino) ethyl dodecanoate and N- (2- (bis (2 hydroxyethyl) amino) ethyl) -N- (2-hydroxyethyl) dodecanamide based on a total weight of the additive mixture and from about 2.5 to about 8% by weight of C12 fatty acid ester (s) and amide (s) derived from the self-condensation product of DEA other than of tris (2-hydroxyethyl) ethylenediamine of formula (III), based on the total weight of the additive mixture.
    The additive mixture described herein can be made by reacting fatty acid (s) with DEA, the reaction being carried out in the presence of a molar excess of DEA over the fatty acid (s) and at a pressure of about 20 to about 500 mBar, for example from about 100 to about 300 mBar at a temperature in the range of about 120 ° C to about 160 ° C, suitably from about 130 ° C to about 150 ° C. The molar ratio of DEA to fatty acid (s) can vary from about 1.2: 1 to about 5: 1, suitably from about 1.5: 1 to about 4: 1 equivalents of DEA per equivalents of acid. To react the fatty acid (s) and DEA, all reactants are placed directly in a reactor and reacted in one step. No alkaline catalyst is needed to carry out the reaction, but an acid catalyst can be used if desired.
    The reaction can be conducted over a period of time ranging from about 6 hours to about 30 hours, such as from about 10 hours to about 26 hours. When the reaction is carried out at a pressure above about 50 mBar, the pressure is then lowered to about 10 to about 50 mBar as soon as an acid number of about 50 mg KOH / g is obtained. The pressure reduction allows water to be removed from the reaction mixture and displaces the reaction equilibrium towards the formation of ester (s) / amide (s). In some embodiments, the fatty acid (s) is lauric acid and / or myristic acid. Lauric acid is a 12-carbon chain fatty acid and myristic acid is a 14-carbon chain fatty acid. One or more particularly useful fatty acids are fatty acids that result from coconut oil. Can be an example
    BE2018 / 0159 fatty acids result from hydrolysis of coconut oil. Once hydrolyzed, this oil is particularly rich in lauric acid.
    Once the reaction is complete, the excess DEA is removed from the reaction product. The reaction is considered complete if the acid number of the reaction mixture is lower than 5 mg KOH / g, for example lower than 3 mg KOH / g, and suitably lower than 2 mg KOH / g. Any excess fatty acid (s) that remain in the reaction product and the DEA can be removed by distilling the reaction product. The reaction product, as made, may contain less than about 0.5 weight percent BHEP, suitably less than about 0.2 weight percent BHEP based on a total weight of the reaction product, and is substantially free of glycerol.
    The concentration of the foregoing additive mixture in the gasoline is usually at least 5 ppm by weight, such as from about 5 to about 1500 ppm by weight, typically from about 40 to about 750 ppm by weight, and preferably from about 50 ppm up to about 500 ppm by weight based on a total weight of a gasoline composition containing the additive mixture. One or more additional optional compounds may be present in the fuel additive compositions of the disclosed embodiments. The fuel additives may include, for example, conventional amounts of octane improvers, corrosion inhibitors, cold flow improvers (CFP additive), pour point lowering agents, solvents, demulsifiers, lubricant additives, additional friction modifiers, amine stabilizers, combustion enhancers, conductivity enhancers, conductivity enhancers, anti-oxidant agents, anti-oxidants, anti-oxidants, anti-oxidizing agents, conductivity enhancers nitrate ignition accelerators, cyclic manganese tricarbonyl compounds, and the like. In some aspects, the additive compositions described herein may contain about 50 weight percent or more, or in other aspects, about 75 weight percent or more, based on the total weight of the additive composition, of one or more of the aforementioned additives. Similarly, the
    BE2018 / 0159 fuels contain suitable amounts of conventional fuel mixing components, such as methanol, ethanol, dialkyl ethers, 2-ethylhexanol, and the like.
    In one embodiment, a fuel additive concentrate may contain the above-described reaction products of a fatty acid, fatty acid ester or mixtures thereof and diethanolamine or self-condensation products of diethanolamine in combination with a carrier fluid and other ingredients selected from one or more detergents selected from Mannich-basic detergents , polyalkylamines, polyalkyl polyamines, polyalkenyl succinimides and quaternary ammonium salt detergents.
    Suitable carrier fluids can be selected from any suitable carrier fluid that is compatible with the gasoline and capable of dissolving or dispersing the components of the additive concentrate. Typically, the carrier fluid is a hydrocarbyl polyether or a hydrocarbon fluid, e.g., a petroleum or synthetic lubricating oil base material comprising mineral oil, synthetic oils such as polyesters or polyethers or other polyols, or hydrocracked or hydroisomerized base material. Alternatively, the carrier fluid may be a distillate boiling in the gasoline range. The amount of carrier fluid in the additive concentrate can vary from 10 to 80% by weight, or from 20 to 75% by weight, or from 30 to 60% by weight based on the total weight of the additive concentrate. Such additive concentrates containing the inventive components, detergent and carrier fluid have been found to remain clear fluids even at temperatures as low as -20 ° C.
    The additive mixture of the present disclosure, including the reaction products of a fatty acid, fatty acid ester, or mixtures thereof and diethanolamine or self-condensation products of diethanolamine described above, and optional additives used in formulating the fuels of this invention can be separately or be blended into the basic fuel in different sub-combinations. In some embodiments, the additive mixture of the present application can be mixed simultaneously in the fuel using an additive concentrate, because it takes advantage of the mutual compatibility and the convenience afforded by the
    BE2018 / 0159 combination of ingredients in the form of an additive concentrate. The use of a concentrate can also reduce the mixing time and reduce the possibility of mixing errors. Accordingly, a fuel additive concentrate may contain from about 5% to about 50% by weight of the fuel additive mixture derived from DEA and fatty acid (s) as described above.
    The fuels of the present application may be applicable to the operation of gasoline and diesel engines. The engines include both stationary engines (eg, engines used in electrical power generation installations, in pumping stations, etc.) and ambulatory engines (eg, engines used as work-producing engines in cars, trucks, roadwork equipment, military vehicles, etc. ).
    EXAMPLES The following examples are illustrative of exemplary embodiments of the disclosure. In these examples, as elsewhere in this application, all parts and percentages are by weight unless otherwise indicated. These examples are intended to be presented for illustration only and are not intended to limit the scope of the invention described herein.
    Comparative Example 1 Comparative Example 1 was prepared by heating 2.7 mole Cg-Cig fatty acid mixture from coconut oil containing from 45 to 56% by weight of lauric acid and from 15 to 23% by weight of myristic acid, with an acid number of 264 up to 277 mg KOH / g and a calculated iodine number of 6-15 and 1.0 mol of diethanolamine (DEA) at 150 ° C with stirring, in a small amount of xylene for about three hours and removing the water that is formed azeotropically. The reaction product contained as main constituent C 8 -C 18 fatty acid diesters and triesters of N, N-bis (2-hydroxyethyl) alkylamides. In a second step, 1.6 moles of diethanolamine were added to the N, N-bis (2-hydroxyethyl) alkylamide
    BE2018 / 0159 ester mixture obtained in the first step and the mixture was heated to 150 ° C with stirring for about two hours, after which the solvent was distilled off to give a brown viscous oil. The progress of the reaction was followed by the removal of aliquots and the measurement of the amide: ester ratio by infrared spectroscopy. Transmission Infrared spectroscopy of the material showed a 2.9: 1 ratio of amide absorption at 1622 cm -1 to ester absorption at 1740 cm -1 . Comparative Example 1 is further described in Table 1.
    Comparative Example 2 Comparative Example 2 was prepared in a single step by mixing 1.0 mol of DEA with 1.1 mol of the same coconut fatty acid as used in Comparative Example 1. A small amount of xylene was added and the mixture was heated to 150 ° C with stirring and the water was removed azeotropically. The use of a small excess of fatty acid ensures that there is a minimal amount of unreacted diethanolamine at the end of the reaction. The progress of the reaction was followed by the removal of aliquots and the measurement of the amide: ester ratio by infrared spectroscopy. Transmission Infrared spectroscopy of the material showed a 2.3: 1 ratio of amide absorption at 1622 cm -1 to ester absorption at 1740 cm -1 . Comparative Example 2 is further described in Table 1.
    Comparative Example 3 Comparative Example 3 was prepared in the same manner as Comparative Example 2, but used isostearic acid with an acid number of 180 to 205 mg KOH / g and a calculated iodine number of 4 instead of coconut fatty acid and used a molar ratio of isostearic acid to diethanolamine of 1.4: 1. Spectroscopy of the material showed a 1.1: 1 ratio of amide absorption at 1622 cm -1 to ester absorption at 1740 cm -1 . Comparative Example 3 is further described in Table 1.
    BE2018 / 0159
    Comparative Example 4 Comparison Example 4 was prepared by the method of US 6,524,353 B2 which discloses a fuel additive composition consisting of the reaction product of (a) diethanolamine; (b) coconut oil; and (c) methyl caprylate; wherein the molar ratio is a: b: c: 1.1, 0: 0.7: 0.3.
    Inventive Additive mixture Four moles of Cs-Cis fatty acid mixture from coconut oil containing 45 to 56% by weight of lauric acid and from 15 to 23% by weight of myristic acid, with an acid number of 264 to 277 mg KOH / g and a calculated iodine number of 6- 15, was reacted with 8 moles of diethanolamine (DEA). The reaction mixture was heated to 150 ° C with stirring and the pressure was reduced to 200 mBar for about 10 hours. Once the acid number reached 50 mg KOH / g, the pressure was lowered to 20 mBar until the acid number became less than 2 mg KOH / g. The reaction product mixture was then distilled to remove excess DEA and optional fatty acid (s). Spectroscopy of the material showed an 8.9: 1 ratio of amide absorption at 1622 cm -1 to ester absorption at 1740 cm -1 . The Inventive Additive Blend is further described in Table 1.
    TABLE 1
    Physical and Chemical Properties of Alkanolamide Fuel Additives
    Example BHEP(% by weight) Free DEA (% by weight) Nitrogen (% by weight) TAN (mg KOH / g) TBN (mg KOH / g) PP(° C) nventive Additive <0.20 <0.4 6.29 0.5 99.6 -9 Comparative Ex. 1 0.32 1.24 4.37 3.1 20.5 +3 Comparative Ex. 2 0.51 0.18 4.57 1.4 51.4 -2 Comparative Ex. 3 0.06 0.3 2.81 1.7 14.6 <-30
    BE2018 / 0159 In the following examples in Tables 2 and 3, a wear test was performed on an E-10 gasoline fuel. All tests contained E10 gasoline and the amount of additives listed in the table. Gasoline packages 1,2 and 3 were three different conventional gasoline additive packages containing Mannich detergents, carrier fluids, corrosion inhibitors, demulsifiers, and the like, plus solvent and a small amount of 2-ethylhexanol. The wear tests were performed using a high frequency reciprocating rig (HFRR) using method ASTM D 6079 which was adapted to allow testing of gasoline at a temperature of 25 ° C. The average of two tests was used to determine the results of the average wear scar diameter reported in tables.
    TABLE 2
    HFRR of Fuel Additive Concentrates
    Example no. Additive Treatment speed, ppm on a weight basis HFRR Average MWSD (μm) 1 E10 gasoline - no additives 0 785 2 Gas package 1 304 768 3 Inventive Additive plus Package 1 457 685 4 Comparative Example 1 plus Package 1 457 753 5 Comparative Example 2 plus Package 1 457 707 6 Comparative Example 3 plus Package 1 457 744 7 Gas package 2 285 758 8 Inventive Additive plus Package 2 438 602 9 Comparative Example 1 plus Package 2 438 692 10 Comparative Example 2 plus Package 2 438 674 11 Comparative Example 3 plus Package 2 438 688
    Example Nos. 1, 2 and 7 in Table 2 provide the HFRR data for the base fuel and the base fuel respectively plus the two Gasoline package concentrates. The HFRR results for the base fuel plus concentrates with the inventive friction modifier (Examples Nos. 3 and 8) were better than the comparative fuel additives (Examples Nos. 4, 5, 6 and 9, 10, 11). The Inventive Additive gave the smallest wear scar in both
    BE2018 / 0159 additive concentrates. Examples Nos. 4, 5 and 6 containing Package 1 and Comparative Examples 1, 2 and 3 respectively had HFRR scars above 700 microns while the Example No. 3 containing the Inventive Additive, had a wear scar of 685 microns. When Petrol Package 2 was used, Example No. 8, which contained the Inventive Additive, a wear scar of just over 600 microns, while Comparative Examples Nr. 9, 10 and 11 had wear scars of more than 670 microns. Accordingly, it was surprising and fairly unexpected that the Inventive Additive would provide lower HFRR wear scars than the examples containing the comparative friction modifiers. The lower wear scars of the additive concentrate containing the Inventive Additive according to the disclosure could not be predicted from the data of Example Nos. 4-6 and 9-11.
    TABLE 3
    HFRR from Inventive Additive with other FMs
    Example no. Gas package 3 Inventive Additive Verg.Ex. 4 GMO Diethoxylated laurylamine Average MWSD (μm) 1 0 0 0 0 0 741 2 304 0 0 0 0 704 3 304 153 0 0 0 575 4 304 0 153 0 0 580 5 304 0 0 153 0 600 6 304 76 0 76 0 566 7 304 153 0 153 0 520 8 304 76 0 0 76 635 9 304 153 0 0 153 639 10 304 0 0 0 153 668 11 304 38 0 76 76 598 12 304 0 0 76 76 629
    Table 3 provides the HFRR data for additive concentrates containing the Inventive Additive (Example No. 3); the Inventive Additive with glycerol monooleate (GMO) (Examples Nos. 6 and 7); and the Inventive Additive
    BE2018 / 0159 with fatty amine diethoxylate (Examples Nos. 8 and 9). The HFRR data for an additive concentrate containing the Inventive Additive and both GMO and the fatty amine diethoxylate is shown in Example no. 11. Table 3 also provides the HFRR data for Comparative Example 4, GMO, and diethoxylated laurylamine. The Inventive Additive had a lower HFRR wear scar (575 microns) than either Comparative Example 4 (580), GMO (600), or diethoxylated laurylamine (668) when tested with equal treatment rate. It was surprising that the combination of the Inventive Additive and GMO produced a lower wear scar (566) than each of the components alone. The combination of the Inventive Additive with diethoxylated laurylamine produced a lower wear scar (635) than diethoxylated laurylamine. In addition, when a small amount of the Inventive Additive was added to the additive concentrate containing both GMO and diethoxylated laurylamine (Example No. 11), the resulting wear scar was better than GMO alone and fatty amine diethoxylates alone.
    In the following table, friction testing was performed on SAE 0W-20 passenger car engine oil that contained all standard engine oil components, but without friction modifiers. The treatment speed of the friction modifier additives was 0.25% by weight in the lubricant. The friction tests were performed using a high frequency reciprocating rig (HFRR) under a load of 4 N with a stroke distance of 1 millimeter at 20 Hz and a temperature of 130 ° C. The friction results are shown in Table 4.
    BE2018 / 0159
    TABLE 4
    HFRR Coefficient of Friction for Fuel Additive Concentrates in Engine Oil
    Example no. Friction coefficient 1 Baseline engine oil 0.146 2 Baseline oil with Comparative Example 1 0.120 3 Baseline oil with Comparative Example 2 0.117 4 Baseline oil with Comparative Example 3 0.134 5 Baseline oil with Comparative Example 4 0.120 6 Baseline oil with Inventive Additive 0.118
    Table 4 provides the HFRR friction for the inventive and comparative additives (Ex. Nos. 2-6) in a formulated engine oil without friction modifiers. In this case, the Inventive Additive (Ex. No. 6) provided a significant reduction in friction compared to the baseline oil (Ex. No. 1). The Inventive Additive (Ex. No. 6) and the comparative fuel additives (Ex. Nos. 2-5) gave similar friction coefficients and were all better than the comparative fuel additive 3 (Ex. No. 4).
    An important feature of the fuel additives of the present disclosure is their stability in fuel additive concentrates at low temperatures. Accordingly, in order to provide sufficient fuel additive to improve wear in the fuel delivery system, as well as to increase the fuel saving of an engine, the additive concentrate containing the foregoing inventive fuel additives must be stable and remain stable at low temperatures for an longer period. It would also be very advantageous if the fuel additives of the present disclosure could improve the stability of fuel additive concentrates containing fatty amethoxylates or partial esters of fatty acids or both at low temperatures. By stable and stability is meant that the additive concentrate remains a clear fluid that is essentially free of sediment or precipitate and completely free of suspended material, flocculant and phase separation at temperatures as low as about -20 ° C
    BE2018 / 0159 during a time period. Samples that are clear and clear (CB) or have a trace of sediment (light sediment) are considered acceptable. In the following examples, the low temperature storage stability of gasoline fuel additive concentrates containing the Inventive Additive 5 was compared with additive concentrates containing the additives of Comparative
    Examples 1-4 contain. Table 5 also contains stability data on fuel additive concentrates containing GMO and diethoxylated laurylamine. Each of the additive concentrates in the following table contained 28.9% by weight of a commonly used Mannich detergent, 19.9% by weight of an aromatic solvent, 1.1% by weight of a Cs branched alcohol, carrier fluids, corrosion inhibitors, demulsifiers and the like. The total treatment speed of the components other than the inventive additives and additional solvent was 67.3% by weight. Approximately 10 grams of each additive concentrate was placed in a glass vial and stored at -20 ° C for 28 days. The vials were visually inspected after 14 and 28 days and evaluated. The results are shown in the table below. The amount of additive and additional solvent (95: 5 weight ratio of aromatic: C 8 branched alcohol) in each of the examples is given in the table below. All quantities are given in weight percentages.
    BE2018 / 0159
    TABLE 5
    Compatibility data
    Ex. Nr. Inventive Additive Verg.Ex. 1 Verg.Ex. 2 Verg.Ex. 3 Verg.Ex. 4 GMO Diethoxyl honors laurylamine Solvent Four weeks at -20 ° C 1 15 0 0 0 0 0 0 17.7 CB 2 0 10 0 0 0 0 0 22.7 Heavy Sediment 3 0 0 10 0 0 0 0 22.7 Heavy Sediment 4 0 0 0 15 0 0 0 17.7 CB 5 0 0 0 0 15 0 0 17.7 Medium Sediment 6 0 0 0 0 10 0 0 22.7 Light Sediment 7 0 0 0 0 0 5 0 27.7 Medium Sediment 8 5 0 0 0 0 5 0 22.7 Light Sediment 9 10 0 0 0 0 5 0 17.7 CB 10 0 10 0 0 0 5 0 17.7 Heavy Sediment 11 0 0 10 0 0 5 0 17.7 Heavy Sediment 12 0 0 0 10 0 5 0 17.7 CB 13 0 0 0 0 0 5 10 17.7 CB 14 0 0 0 0 0 0 10 22.7 CB 15 10 0 0 0 0 0 10 12.7 CB 16 0 10 0 0 0 0 10 12.7 Heavy Sediment 17 0 0 10 0 0 0 10 12.7 Heavy Sediment 18 0 0 0 10 0 0 10 12.7 CB 19 0 0 0 0 0 0 17.5 15.2 Solid 20 2.5 0 0 0 0 0 17.5 12.7 Light Sediment 21 0 0 0 2.5 0 0 17.5 12.7 SolidTwo weeks at -20 ° C 22 2.5 0 0 0 0 0 20 10.2 CB 23 0 0 0 2.5 0 0 20 10.2 Heavy Sediment 24 10 0 0 0 0 10 0 12.7 CB 25 0 0 0 10 0 10 0 12.7 Medium Sediment 26 0 0 0 0 10 10 0 12.7 Medium Sediment 27 0 0 0 0 0 10 0 22.7 Medium Sediment
    BE2018 / 0159 As shown in Table 5, the fuel additive concentrates containing the Inventive Additive (Ex. Nos. 1, 9 and 15) remained clear and clear (CB) after four weeks at a temperature of -20 ° C while the additive concentrates containing Comparative Examples 1 and 2 (Ex. Nos. 2, 3, 10, 11, 16 and 17) had a heavy sediment at -20 ° C after four weeks. Comparative Example 3, which is the fuel additive made from a branched fatty acid using the non-inventive process, provided stable fuel additive concentrates that remained liquid at low temperatures (Ex. Nos. 4, 12 and 18). However, the fuel additive concentrates containing Comparative Example 3 and high levels of GMO or diethoxylated laurylamine became hazy within one week and unstable after two weeks (Ex. Nos. 21, 23 and 25). The Inventive Additive thus considerably increases the stability of fuel additive concentrates that would otherwise be unstable (Ex. Nos. 7,19 and 27) and allows the fuel additives to be used in concentrates that are stable at -20 ° C (Ex. Nos. 9) , 20 and 24). Comparative Example 4 is a mixture of alkanolamides made from coconut oil and methyl caprylate using the method described in U.S. Pat. 6,524,353 B2. The use of methyl caprylate in the reaction mixture improves the low temperature performance of fuel additive product when mixed into concentrates at 50% with aromatic solvent. However, the fuel additive concentrates made from Comparative Example 4 (Ex. Nos. 5 and 26) were not stable at -20 ° C when formulated with the fully formulated concentrates.
    Accordingly, based on the foregoing stability tests, the fuel additive concentrates made with the Inventive Additive had satisfactory low temperature stability and the Inventive Additive can be used to improve the low temperature storage stability of a fuel additive composition containing a fatty amine ethoxylate or GMO or both.
    In the following examples, the low temperature storage stability of gasoline fuel additive concentrates containing the Inventive Additive
    BE2018 / 0159, compared to additive concentrates containing mixtures of N, Nbis (2-hydroxyethyl) alkylamides (I), also called Coco-DEA and the coconut fatty acid esters and amides derived from the self-condensation products of two diethanolamines; 2 - ((2- (bis (2-hydroxyethyl) amino) ethyl) amino) ethyl alkanoate and N- (2- (bis (2-hydroxyethyl) amino) ethyl) -N- (2-hydroxyethyl) alkyl amide (also Coco-dimer called DEA). The Coco-DEA was made from coconut fatty acid and purified to remove all products derived from DEA dimers, trimers and higher oligomers. Similarly, the Coco-dimer DEA was made from coconut fatty acid and purified to remove all Coco-DEA and products derived from DEA trimers and higher oligomers. Each of the additive concentrates in the following table contained the same additive components as were used in Table 5. The treatment rates of the Coco-DEA and Coco-dimeric DEA mixtures as well as the treatment rate of the Inventive Additive was 20% by weight. Approximately 10 grams of each additive concentrate was placed in a glass vial and stored at -20 ° C for 28 days. The vials were visually inspected after 7 and 28 days and evaluated. The results are shown in the table below.
    TABLE 6
    Relative compatibility data
    CocoDEA (% by weight) Coco-dimer DEA (% by weight) 7 days at -20 ° C 28 days at -20 ° C 100 0 Heavy Sediment Solid 95 5 Heavy Sediment Fixed sof 90 10 Heavy Sediment Heavy Sediment 85 15 Light Sediment Heavy Sediment 80 20 CB Light Sediment 75 25 CB Light Sediment Inventive Additive CB CB
    BE2018 / 0159 The data show the beneficial effect that the Coco dimer DEA has on the low temperature compatibility of the additive concentrates. Above 15% addition, the additive concentrate is clear and clear on day 7, while pure CocoDEA already shows heavy sediment (15% treatment rate shows light sediment). At 28 days the addition of Coco-dimer DEA shows a light sediment at 25% with the lower treatment rate showing heavy sediment or even coagulation at 0% and 5%. Only the Inventive Additive is still ready and clear after 28 days. In all cases, the Inventive Additive performs better than the Coco-dimer DEA. Without wishing to be bound by theory, it may be that although it contains Coco-DEA Inventive Additive, it also contains trimers ester / amides and other DEA oligomers that improve cold temperature properties.
    In addition, the Inventive Additive was evaluated for effectiveness in reducing fuel consumption in gasoline engines. The tests were performed using the US Federal Test Procedure FTP-75 on chassis dynamometers under controlled temperature and humidity conditions, while the transient phase driving time schedule (Bag 2) was used in triplicate.
    TABLE 7
    Test the chassis dynamometer: increase in fuel savings
    Inventive Additive(ppm by weight)% ElevationFuel saving 0 Gasoline plus no treatment additive 0 228 2010 Ford F150 4.6L / V8 0.71 342 2015 Volkswagen Golf 1.8L / DI 0.84
    BE2018 / 0159 As shown in the previous table, the Inventive Additive in a fuel additive composition at 228 and 342 ppm provided significant fuel-saving increases compared to the basic fuel composition that was free of the Inventive Additive. Accordingly, the Inventive Additive offers, in addition to friction and wear reduction and low temperature stability, fuel-saving improvements in gasoline fuels.
    An engine test that measures fuel injector deposits (referred to as DIG test) was conducted according to a procedure described in SAE Int. J Fuels Lubr. 10 (3): 2017 A general method for fouling injectors in gasoline-injected vehicles and the effects of deposits on vehicle performance. A mathematical value of Long Term Fuel Trim (LTFT) was used to measure the effectiveness of additives for cleaning the injectors in a gasoline engine by performing a contamination phase until the LTFT is 9-10% higher than at the start of the test (approximately 6,000 miles), followed by a cleaning phase (approximately 2,000 miles). The lower the% LTFT at 8,000 miles, the more effective the additive is when cleaning dirty injectors. For the DIG test, a 2012 Kia Optima (L-4, 2.4L engine) was used, equipped with a Direct Injection Fuel Management System. The Inventive Additive was used at 67 ppm in a formulation that did not contain detergent. The results are shown in the following table.
    TABLE 8
    DIG test: Injector deposit cleaning
    Additive Treatment speed(ppm) LTFT% after pollution % Improvement after cleaning Inventive 67 9.2 98
    BE2018 / 0159 The inventive example showed a significant cleaning of dirty injectors for a DIG engine at a relatively low treatment speed.
    The pour point data in Table 1 shows that the Inventive Additive had a lower pour point than both Comparative Example 1 (3 ° C) and Comparative Example 2 (-2 ° C). The pouring point of the Inventive Additive is -9 ° C when fatty acids obtained from coconut oil are used. When pure lauric acid is used to make the additive mixture described herein, a pour point of -15 ° C is observed and the pour point drops to -34 ° C when pure caprylic acid is used. It is well known to those skilled in the art that shorter fatty acid chains result in better cold flow properties. Coconut oil has some palmitic acid and stearic acid, which increases the pouring point, while caprylic acid (Cg) has a shorter hydrocarbon chain than lauric acid (Cl2). It was surprising and unexpected that the pouring point of the Inventive Additive would be lower than Comparative Examples 1 and 2 when all three additives use the same fatty acid to make the additive.
    It is noted that, as used in this specification and the appended claims, the singular forms include one, the, and also the plural reference, unless expressly and unambiguously limited to one sponsor. Thus, for example, reference to an antioxidant includes two or more different antioxidants. As used herein, the term include and its grammatical variants are intended to be non-limiting so that listing of items in a list does not occur to the exclusion of other similar items that can be replaced or added to the listed items.
    For the purposes of this specification and appended claims, unless otherwise indicated, all numbers that include quantities, percentages or ratios, and other numerical values used in the specification and claims, should be understood as modified in all cases by the term. about. Accordingly, unless otherwise indicated, the numerical parameters set forth in the following description and appended claims are approximations that may vary depending on the desired properties that are desired by the current disclosure.
    BE2018 / 0159. At the very least, and not as an attempt to limit the application of the doctrine of equivalents to the scope of the claims, each numerical parameter must be interpreted at least in the light of the number of significant figures reported and the application of ordinary 5 rounding techniques.
    Although specific embodiments have been described, alternatives, modifications, variations, improvements, and substantial equivalents that are or may be unforeseeable at this time may occur to applicants or others skilled in the art. Accordingly, the appended claims as submitted and as they may be amended are intended to include all such alternatives, modifications, variations, improvements, and substantial equivalents.
    权利要求:
    Claims (15)
    [1]
    CONCLUSIONS
    A fuel additive concentrate for gasoline comprising an aromatic solvent and a mixture comprising (i) N, N-bis (2-hydroxyethyl) alkylamide, (ii) 2 - ((2- (bis (2-hydroxyethyl) amino) ethyl) amino) ethyl alkanoate and N- (2- (bis (2-hydroxyethyl) -amino) ethyl) -N- (2-hydroxyethyl) alkylamide, and (iii) fatty acid ester (s) and amide (s) derived from a self-condensation product of diethanolamine (DEA) that contains at least 3 amino groups in which a weight ratio of (i) to (ii) to (iii) ranges from about 8: 2: 0 to about 2: 5: 3 and wherein the fuel additive mixture is substantially free of glycerol and remains liquid at a temperature to about -20 ° C.
    [2]
    The fuel additive concentrate according to claim 1, wherein the mixture comprises less than 3% by weight of N, N'-bis (2-hydroxyethyl) piperazine based on the total weight of the additive mixture, or wherein the mixture is less than 0.5% by weight % N, N'-bis (2-hydroxyethyl) piperazine based on the total weight of the additive mixture, or wherein the mixture comprises from about 5 to about 30% by weight of fatty acid ester (s) and amide (s), derived of a DEA self-condensing product containing at least 3 amino groups based on the total weight of the additive mixture, or wherein the alkyl groups of the amide (s) and ester (s) contain from 8 to 18 carbon atoms.
    [3]
    The fuel additive concentrate according to claim 2, wherein from about 45% to about 55% by weight of the alkyl groups in the amide (s) and ester (s) are dodecyl groups.
    [4]
    The fuel additive concentrate of claim 1, further comprising one or more detergents and one or more carrier fluids, or further comprising a
    BE2018 / 0159 friction modifier selected from the group consisting of partial esters of fatty acids and polyhydroxy alcohols, N, N-bis (hydroxylalkyl) alkylamine, and mixtures thereof, wherein a weight ratio of the friction modifier to the mixture in the concentrate varies from about 10: 1 until about 1:10.
    [5]
    A gasoline fuel composition for reducing wear of the fuel system component and engine friction and improving the purity of the injector, comprising:
    A) gasoline and
    B) containing a fuel additive mixture
    a) N, N-bis (2-hydroxyethyl) alkylamide,
    b) 2 - ((2- (bis (2-hydroxyethyl) amino) ethyl) amino) ethyl alkanoate and N- (2- (bis (2-hydroxyethyl) amino) ethyl) -N- (2-hydroxyethyl) alkylamide, and
    c) fatty acid ester (s) and amide (s) derived from a diethanolamine (DEA) self-condensing product containing at least 3 amino groups, the alkyl groups of the amide (s) and ester (s) containing from 8 to 18 carbon atoms and wherein a weight ratio of (a) to (b) to (c) in the fuel additive mixture ranges from about 8: 2: 0 to about 2: 5: 3 and wherein the fuel additive mixture is substantially free of glycerin and remains liquid at a temperature to around -20 ° C.
    [6]
    The gasoline fuel composition of claim 5, wherein the fuel additive mixture comprises less than 0.5% by weight of N, N'-bis (2-hydroxyethyl) piperazine based on the total weight of the additive blend, or wherein the fuel additive blend comprises from about 5 to about 30% by weight of fatty acid ester (s) and / or amide (s) derived from a self-condensing product from DEA containing at least 3 amino groups based on the total weight of the additive blend.
    BE2018 / 0159
    [7]
    The gasoline fuel composition of claim 6, wherein the gasoline fuel composition comprises from about 10 to about 1500 ppm by weight of the fuel additive mixture based on the total weight of the fuel composition.
    [8]
    A method for reducing wear and engine friction, comprising:
    providing gasoline containing a wear-reducing additive blend consisting essentially of:
    a) N, N-bis (2-hydroxyethyl) alkylamide,
    b) 2 - ((2- (bis (2-hydroxyethyl) amino) ethyl) amino) ethyl alkanoate and N (2- (bis (2-hydroxyethyl) amino) ethyl) -N- (2-hydroxyethyl) alkylamide, and
    c) fatty acid ester (s) and amide (s) derived from a diethanolamine (DEA) self-condensing product containing at least 3 amino groups, the additive mixture being substantially free of glycerin and a weight ratio of (a) to (b) to (c) ) ranges from about 8: 2: 0 to about 2: 5: 3;
    combining the additive blend with gasoline to provide a fuel composition; and operating the engine on the fuel composition.
    [9]
    The method of claim 8, wherein the gasoline contains from about 10 to about 1500 ppm by weight of a fuel additive concentrate comprising the additive blend based on the total weight of the gasoline and the fuel additive concentrate.
    [10]
    The method of claim 9, wherein the additive concentrate comprises from about 10 to about 90% by weight of the additive blend based on a total weight of the additive concentrate, or wherein the additive concentrate
    BE2018 / 0159 fuel additive concentrate remains liquid at a temperature of up to -20 ° C.
    [11]
    The method of claim 8, wherein the amount of fatty acid ester (s) and amide (s) derived from a self-condensing product of DEA containing at least 3 amino groups in the additive mixture ranges from about 5 to about 30% by weight. of the total weight of the additive mixture, and / or wherein the alkyl groups of the amide (s) and ester (s) contain from 8 to 18 carbon atoms.
    [12]
    A method for improving the injector performance of a fuel-injected gasoline engine, comprising:
    providing gasoline containing an injector-cleaning additive mixture consisting essentially of:
    a) N, N-bis (2-hydroxyethyl) alkylamide,
    b) 2 - ((2- (bis (2-hydroxyethyl) amino) ethyl) amino) ethyl alkanoate and N (2- (bis (2-hydroxyethyl) amino) ethyl) -N- (2-hydroxyethyl) alkylamide, and
    c) fatty acid ester (s) and amide (s) derived from a diethanolamine (DEA) self-condensing product containing at least 3 amino groups, the additive mixture being substantially free of glycerin and a weight ratio of (a) to (b) to (c) ) ranges from about 8: 2: 0 to about 2: 5: 3;
    combining the additive mixture with gasoline to provide a fuel composition; and operating the engine on the fuel composition.
    [13]
    The method of claim 12, wherein the gasoline comprises from about 10 to about 1500 ppm by weight of a fuel additive concentrate comprising the additive mixture based on the total weight of the gasoline and the fuel additive concentrate.
    BE2018 / 0159
    [14]
    The method of claim 13, wherein the additive concentrate comprises from about 10 to about 90% by weight of the additive mixture based on the total weight of the additive concentrate, or wherein the fuel additive concentrate remains liquid at a temperature of up to about
    5-20 ° C.
    [15]
    The method of claim 12, wherein the amount of fatty acid ester (s) and amide (s) derived from a DEA self-condensing product containing at least 3 amino groups in the additive mixture ranges from about 5
    10 to about 30% by weight of the total weight of the additive mixture, and / or wherein the alkyl groups of the amide (s) and ester (s) contain from 8 to 18 carbon atoms.
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    同族专利:
    公开号 | 公开日
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    GB2569897A|2019-07-03|
    GB201821249D0|2019-02-13|
    BR102018077042A2|2019-09-17|
    CA3028395A1|2019-06-04|
    EP3505603A1|2019-07-03|
    CN109971518A|2019-07-05|
    BE1025932A1|2019-08-09|
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    法律状态:
    2019-10-10| FG| Patent granted|Effective date: 20190919 |
    2021-09-03| MM| Lapsed because of non-payment of the annual fee|Effective date: 20201231 |
    优先权:
    申请号 | 申请日 | 专利标题
    US15/855,011|US10011795B1|2017-12-27|2017-12-27|Fuel additive mixtures and fuels containing them|
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