US20030163952A1 - Compositions - Google Patents

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US20030163952A1
US20030163952A1 US10/220,079 US22007903A US2003163952A1 US 20030163952 A1 US20030163952 A1 US 20030163952A1 US 22007903 A US22007903 A US 22007903A US 2003163952 A1 US2003163952 A1 US 2003163952A1
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Prior art keywords
fuel composition
composition according
alcohol
fatty acid
fuel
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US10/220,079
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Alan Rae
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O2Diesel Europe Ltd
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AAE Technologies International PLC
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/143—Organic compounds mixtures of organic macromolecular compounds with organic non-macromolecular compounds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/185—Ethers; Acetals; Ketals; Aldehydes; Ketones
    • C10L1/1852—Ethers; Acetals; Ketals; Orthoesters
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/19—Esters ester radical containing compounds; ester ethers; carbonic acid esters
    • C10L1/191—Esters ester radical containing compounds; ester ethers; carbonic acid esters of di- or polyhydroxyalcohols
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/192—Macromolecular compounds
    • C10L1/198—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
    • C10L1/1985—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid polyethers, e.g. di- polygylcols and derivatives; ethers - esters
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/22—Organic compounds containing nitrogen
    • C10L1/222—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
    • C10L1/2222—(cyclo)aliphatic amines; polyamines (no macromolecular substituent 30C); quaternair ammonium compounds; carbamates
    • C10L1/2225—(cyclo)aliphatic amines; polyamines (no macromolecular substituent 30C); quaternair ammonium compounds; carbamates hydroxy containing

Definitions

  • This invention relates to a novel fuel composition and to methods of their preparation and use.
  • Diesel fuel is an important petroleum product and is depended upon for powering the engines of ships, trains, trucks, etc. Since petroleum is a non-renewable resource and because the burning of diesel in an internal combustion engine produces high levels of pollutants, especially particulates, much effort has gone into the development of alternative fuels from renewable sources.
  • Biodiesel has a much higher cloud point (about 0° C.) than petroleum diesel and also has a much higher pour point (about ⁇ 2° C.).
  • cloud point about 0° C.
  • pour point about ⁇ 2° C.
  • Biodiesel fuels are also known to cause much more wear and tear on engines and have higher particulate emissions than conventional petroleum diesel fuel.
  • a fuel composition comprising biodiesel and a surfactant, characterised in that the surfactant comprises a mixture of an alkanolamide, an alkoxylated alcohol and an alkoxylated fatty acid or a derivative thereof.
  • the diesel component of the fuel composition can comprise up to 100% v/v biodiesel.
  • the diesel component is preferably a mixture of petroleum diesel and biodiesel.
  • Such a mixture can comprise up to 20% v/v biodiesel, for example from 1 to 20% v/v, preferably from 5 to 20% v/v, more preferably from 10 to 20% v/v.
  • the fuel composition also comprises an alcohol e.g. an alkanol, such as ethanol.
  • an alcohol e.g. ethanol
  • the alcohol may be present in an amount of from 1 to 10% v/v, preferably 5 to 10% v/v and more preferably 1 to 3% v/v.
  • the alkanolamide is preferably an ethanolamide and more preferably a diethanolamide.
  • the diethanolamides and particularly the super diethanolamides are preferably a diethanolamide in which the nitrogen is substituted by an alkyl substituent e.g. alkyl C 5 to C 20 , preferably C 8 to C 18 , more preferably C 10 to C 18 .
  • the most preferred diethanolamide is a C 18 substituent i.e. oleic diethanolamide.
  • super amide normally refers to an amide derived by reaction of substantially stoichiometric proportions of diethanolamine with a fatty ester, typically a methyl or glyceryl ester.
  • the alkoxylated alcohol is preferably an ethoxylated alcohol. It is essential that the ethoxylated alcohol is an oil soluble alcohol. Therefore, alkanols are preferred and these may be primary, secondary or tertiary alkanols and especially primary alkanols. As the oil solubility of the alcohol may vary with the carbon chain length of the ethoxylated alkanol, the alkanol is preferably a C 5 to C 22 alkanol, more preferably C 5 to C 15 alkanol.
  • the ethoxylated alcohol may comprise a mixture of alkanols or a mixture in which one alkanol will predominate.
  • the most preferred alkanol is predominantly a C 9 to C 11 alkanol.
  • the degree of ethoxylation of the alcohol may be varied and the oil solubility will, generally, decrease with the increase in the degree of ethoxylation. It is preferred that the ethoxylate to alcohol ratio is greater than 2. More preferably, the ethoxylate to alcohol ratio is from between 1 and 10, preferably between 1 and 5, more preferably between 1 and 3 and especially between 2 and 3.
  • a commercially available ethoxylated alcohol is especially preferred in which the ethoxylate to alcohol ratio is 2.75. Such an alcohol ethoxylate is available as NEODOL 91/2.5.
  • the fatty acid ethoxylate may comprise any conventionally known fatty acid ethoxylate or a derivative thereof.
  • the fatty acid ethoxylate may be derived from a fatty acid having from 8 to 20 carbon atoms, preferably from 10 to 18.
  • the fatty acid may be a saturated or unsaturated fat.
  • alkoxylated fatty acid or a derivative thereof we mean a derivative of the acid, for example, an ester e.g. an alkyl ester.
  • the most preferred fatty acid is an unsaturated fatty acid and especially C 18 , oleic acid or a derivative thereof, such as an oleate ester, e.g. an alkyl C 1 to C 10 oleate.
  • Derivatives which may be mentioned include an ethyl oleate or a methyl oleate.
  • the fatty acid when ethanol is present then the fatty acid is greater than C 15 and especially oleic.
  • the degree of ethoxylation is chosen to optimise performance in the blend with the other two selected surfactants and may be from 1 to 20, but more preferably from 5 to 18.
  • a suitable product within this range would be, for example that derived from the addition of 7 molecules of ethylene oxide to 1 mole of oleic acid.
  • the values will depend on the length of the hydrophilic chain, typically an ethoxylate chain.
  • the length of the chain will increase the extent of solubilisation because of a greater ability to solubilise.
  • a blend of surfactants is preferred, preferably by selecting one with an HLB appropriate to the fuel, say 10 to 18 for hydrocarbon fuel, most preferably 13.
  • an HLB value of the surfactant is between 3 and 7, most preferably about 4.
  • the invention has the ability to unify the HLB requirements of any liquid fuel which in turn allows for one dose to be used in any fuel from C5 carbon chains up.
  • the benefit being the amount of treatment directly related to the co-solvency ability.
  • the ethoxylate of the fatty acid makes up about 25% by volume of the additive and further preferably the alcohol ethoxylate comprises 50% by volume of the additive.
  • An additive of the invention may be added to a hydrocarbon fuel, e.g. diesel, petrol or alcohol, such as ethanol which may or may not be contaminated with water.
  • a hydrocarbon fuel e.g. diesel, petrol or alcohol, such as ethanol which may or may not be contaminated with water.
  • the invention is seen to particularly good effect when added to synthetic fuels based on low fraction oils.
  • the presence of the additive of the invention ensures that the fuel composition forms a consistent stable homogenous composition and creates a monolayer simultaneously a result of which leads to a better more complete burn which reduces pollution and increases miles per gallon.
  • the concentration of the additive in the fuel can be very low, typically the additive to fuel ratio may be of the order of 0.5-50:1200, preferably about 0.5-50:1000, more preferably 1-30:1000 and most preferably 30:1000. There appears to be no technical or economic benefit in adding more unless a co-solvent dual action is required, when the priority will be dosage against performance.
  • the fuel is considered to comprise the sum of any petroleum diesel, biodiesel and alcohol present in the composition.

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

There is described a fuel composition comprising biodiesel and a surfactant, characterised in that the surfactant comprises a mixture of an alkanolamide, an alkoxylated alcohol and an alkoxylated fatty acid or a derivative thereof. More particularly there is described a fuel composition in which the diesel component is a mixture of biodiesel and petroleum diesel, e.g. up to 20% v/v biodiesel. There is also described a method of running an internal combustion engine comprising the use of a fuel according to claim 1.

Description

  • This invention relates to a novel fuel composition and to methods of their preparation and use. [0001]
  • Diesel fuel is an important petroleum product and is depended upon for powering the engines of ships, trains, trucks, etc. Since petroleum is a non-renewable resource and because the burning of diesel in an internal combustion engine produces high levels of pollutants, especially particulates, much effort has gone into the development of alternative fuels from renewable sources. [0002]
  • Since the 1930's biodiesel fuel has been considered as an alternative to petroleum based diesel. In some cases vegetable oils have been added to petroleum diesel to try and at least mitigate some of the problems with petroleum diesel. Such vegetable oil may originate from a variety of sources, such as soybean oil, rape seed oil, palm oil and sunflower oil. [0003]
  • However, the use of biodiesel or petroleum diesel/biodiesel mixtures presents a number of difficulties. Biodiesel has a much higher cloud point (about 0° C.) than petroleum diesel and also has a much higher pour point (about −2° C.). Thus, the widespread use of biodiesel fuels does not appear practical until, inter alia, the low temperature viscosity issues of the fuel are addressed. Biodiesel fuels are also known to cause much more wear and tear on engines and have higher particulate emissions than conventional petroleum diesel fuel. [0004]
  • Attempts have been made to overcome these disadvantages by using emulsions of alcohols and vegetable oils, often including the use of a surfactant. However, these emulsions are not particularly stable at low temperatures and the alcohol has a tendency to absorb water. [0005]
  • We have now surprisingly found a fuel composition which overcomes or mitigates the problems of prior art fuels.[0006]
  • Thus according to the invention we provide a fuel composition comprising biodiesel and a surfactant, characterised in that the surfactant comprises a mixture of an alkanolamide, an alkoxylated alcohol and an alkoxylated fatty acid or a derivative thereof. [0007]
  • The diesel component of the fuel composition can comprise up to 100% v/v biodiesel. However, the diesel component is preferably a mixture of petroleum diesel and biodiesel. Such a mixture can comprise up to 20% v/v biodiesel, for example from 1 to 20% v/v, preferably from 5 to 20% v/v, more preferably from 10 to 20% v/v. [0008]
  • In a preferred embodiment the fuel composition also comprises an alcohol e.g. an alkanol, such as ethanol. When an alcohol is present the alcohol, e.g. ethanol, may be present in an amount of from 1 to 10% v/v, preferably 5 to 10% v/v and more preferably 1 to 3% v/v. [0009]
  • In the surfactant composition, the alkanolamide is preferably an ethanolamide and more preferably a diethanolamide. Especially preferred are the diethanolamides and particularly the super diethanolamides. By the term super diethanolamide we mean a diethanolamide in which the nitrogen is substituted by an alkyl substituent e.g. alkyl C[0010] 5 to C20, preferably C8 to C18, more preferably C10 to C18. The most preferred diethanolamide is a C18 substituent i.e. oleic diethanolamide. The term super amide normally refers to an amide derived by reaction of substantially stoichiometric proportions of diethanolamine with a fatty ester, typically a methyl or glyceryl ester.
  • There are three commercial routes to alkanolamides; [0011]
  • Acid+alkanolamine=alkanolamide+water [0012]
  • Plant or animal oil (triglyceride)+alkanolamine alkanolamide+glycerol [0013]
  • Methyl ester+alkanolamine=alkanolamide+methanol [0014]
  • These are listed in order of increasing product quality. The route via the acid often uses an excess of alkanolamine to produce a product higher in amide than is obtainable from the acid if a stoichiometric ratio is used; these products are sometimes referred to as Kritchevsky amides. [0015]
  • The alkoxylated alcohol is preferably an ethoxylated alcohol. It is essential that the ethoxylated alcohol is an oil soluble alcohol. Therefore, alkanols are preferred and these may be primary, secondary or tertiary alkanols and especially primary alkanols. As the oil solubility of the alcohol may vary with the carbon chain length of the ethoxylated alkanol, the alkanol is preferably a C[0016] 5 to C22 alkanol, more preferably C5 to C15 alkanol. The ethoxylated alcohol may comprise a mixture of alkanols or a mixture in which one alkanol will predominate. Thus, the most preferred alkanol is predominantly a C9 to C11 alkanol. In addition the degree of ethoxylation of the alcohol may be varied and the oil solubility will, generally, decrease with the increase in the degree of ethoxylation. It is preferred that the ethoxylate to alcohol ratio is greater than 2. More preferably, the ethoxylate to alcohol ratio is from between 1 and 10, preferably between 1 and 5, more preferably between 1 and 3 and especially between 2 and 3. A commercially available ethoxylated alcohol is especially preferred in which the ethoxylate to alcohol ratio is 2.75. Such an alcohol ethoxylate is available as NEODOL 91/2.5.
  • The fatty acid ethoxylate may comprise any conventionally known fatty acid ethoxylate or a derivative thereof. Thus the fatty acid ethoxylate may be derived from a fatty acid having from 8 to 20 carbon atoms, preferably from 10 to 18. The fatty acid may be a saturated or unsaturated fat. By the term “alkoxylated fatty acid or a derivative thereof we mean a derivative of the acid, for example, an ester e.g. an alkyl ester. The most preferred fatty acid is an unsaturated fatty acid and especially C[0017] 18, oleic acid or a derivative thereof, such as an oleate ester, e.g. an alkyl C1 to C10 oleate. Derivatives which may be mentioned include an ethyl oleate or a methyl oleate. In one embodiment of the invention, when ethanol is present then the fatty acid is greater than C15 and especially oleic.
  • The degree of ethoxylation is chosen to optimise performance in the blend with the other two selected surfactants and may be from 1 to 20, but more preferably from 5 to 18. A suitable product within this range would be, for example that derived from the addition of 7 molecules of ethylene oxide to 1 mole of oleic acid. [0018]
  • The preferred additive of this invention is a non-ionic surfactant and preferably a blend of surfactants. It is a preferred feature of this invention that the surfactants be selected by their nature and concentration that the additive (as well as any water or other non-fuel liquid present) be solubilised within the fuel. For this purpose it is convenient to have regard to the hydrophilic-lipophilic balance (HLB) of the surfactant, the value being calculated according to the expression. [0019] HLB = mol .   wt   of   hydrophilic   chain × 20 total   mol .   wt
    Figure US20030163952A1-20030904-M00001
  • The values will depend on the length of the hydrophilic chain, typically an ethoxylate chain. The length of the chain will increase the extent of solubilisation because of a greater ability to solubilise. [0020]
  • As with the compositions described in WO98/17745, a blend of surfactants is preferred, preferably by selecting one with an HLB appropriate to the fuel, say 10 to 18 for hydrocarbon fuel, most preferably 13. In the case of an alcohol the HLB value of the surfactant is between 3 and 7, most preferably about 4. [0021]
  • The invention has the ability to unify the HLB requirements of any liquid fuel which in turn allows for one dose to be used in any fuel from C5 carbon chains up. The benefit being the amount of treatment directly related to the co-solvency ability. [0022]
  • Preferably the ethoxylate of the fatty acid makes up about 25% by volume of the additive and further preferably the alcohol ethoxylate comprises 50% by volume of the additive. [0023]
  • An additive of the invention may be added to a hydrocarbon fuel, e.g. diesel, petrol or alcohol, such as ethanol which may or may not be contaminated with water. The invention is seen to particularly good effect when added to synthetic fuels based on low fraction oils. [0024]
  • The presence of the additive of the invention ensures that the fuel composition forms a consistent stable homogenous composition and creates a monolayer simultaneously a result of which leads to a better more complete burn which reduces pollution and increases miles per gallon. [0025]
  • The concentration of the additive in the fuel can be very low, typically the additive to fuel ratio may be of the order of 0.5-50:1200, preferably about 0.5-50:1000, more preferably 1-30:1000 and most preferably 30:1000. There appears to be no technical or economic benefit in adding more unless a co-solvent dual action is required, when the priority will be dosage against performance. In the aforementioned ratios the fuel is considered to comprise the sum of any petroleum diesel, biodiesel and alcohol present in the composition. [0026]
  • We also provide a method of running an engine adapted to use a diesel-based fuel, comprising adding to the petroleum diesel and biodiesel mixture a miscible additive selected to solubilise the fuel and the additive so eliminating the deposit of by-products formed during the combustion of the fuel. [0027]

Claims (41)

1. A fuel composition comprising biodiesel and a surfactant, characterised in that the surfactant comprises a mixture of an alkanolamide, an alkoxylated alcohol and an alkoxylated fatty acid or a derivative thereof.
2. A fuel composition according to claim 1 characterised in that the diesel component is a mixture of biodiesel and petroleum diesel.
3. A fuel composition according to claim 1 characterised in that the fuel composition comprise up to 20% V/V biodiesel.
4. A fuel composition according to claim 1 characterised in that a non-alkoxylated alcohol is also present.
5. A fuel composition according to claim 4 characterised in that the alcohol is an alkanol.
6. A fuel composition according to claim 5 characterised in that the alkanol is ethanol.
7. A fuel composition according to claim 1 characterised in that the fuel composition comprise from 1 to 20% v/V of a non-alkoxylated alcohol.
8. A fuel composition according to claim 4 characterised in that the amount of alcohol present is from 1 to 10% v/v.
9. A fuel composition according to claim 8 characterised in that the amount of alcohol present is from 5 to 10% v/v.
10. A fuel composition according to claim 1 characterised in that the alkanolamide is an ethanolamide
11. A fuel composition according to claim 1 characterised in that the alkanolamide is a diethanolamide.
12. A fuel composition according to claim 11 characterised in that the diethanolamides are super diethanolamides.
13. A fuel composition according to claim 11 characterised in that the nitrogen in the diethanolamide is substituted by an alkyl C5 to C20 substituent.
14. A fuel composition according to claim 13 characterised in that the diethanolamide is substituted by an alkyl C8 to C18 substituent.
15. A fuel composition according to claim 14 characterised in that the diethanolamide is substituted by an alkyl C10 to C18 substituent.
16. A fuel composition according to claim 15 characterised in that the diethanolamide is a lauryl diethanolamide.
17. A fuel composition according to claim 15 characterised in that the alkyl substituent is an unsaturated substituent.
18. A fuel composition according to claim 17 characterised in that the diethanolamide is oleic diethanolamide.
19. A fuel composition according to claim 1 characterised in that the alkoxylated alcohol is an ethoxylated alcohol.
20. A fuel composition according to claim 19 characterised in that the ethoxylated alcohol is an oil soluble alcohol.
21. A fuel composition according to claim 19 characterised in that the ethoxylated alcohol is an ethoxylated alkanol.
22. A fuel composition according to claim 21 characterised in that the ethoxylated alcohol is a primary alkanol.
23. A fuel composition according to claim 1 characterised in that the alkanol is C5 to C22 alkanol.
24. A fuel composition according to claim 21 characterised in that the ethoxylated alcohol comprises a mixture of alkanols in which one alkanol predominates.
25. A fuel composition according to claim 21 characterised in that the predominate alkanol is a C9 to C11 alkanol.
26. A fuel composition according to claim 25 characterised in that the ethoxylate to alcohol ratio is from between 1 and 10.
27. A fuel composition according to claim 26 characterised in that the ethoxylate to alcohol ratio is from between 1 and 5.
28. A fuel composition according to claim 27 characterised in that the ethoxylate to alcohol ratio is from between 2 and 3.
29. A fuel composition according to claim 28 characterised in that the ethoxylate to alcohol ratio is 2.75.
30. A fuel composition according to claim 29 characterised in that the ethoxylated alcohol is NEODOL 91/2.5.
31. A fuel composition according to claim 1 characterised in that the fatty acid group is a C8 to C20 fatty acid or a derivative thereof.
32. A fuel composition according to claim 31 characterised in that the fatty acid group is a C10 to C18 fatty acid or a derivative thereof.
33. A fuel composition according to claim 32 characterised in that the fatty acid group is a C14 fatty acid (myristic acid) or a derivative thereof.
34. A fuel composition according to claim 31 characterised in that the fatty acid is an unsaturated fatty acid or a derivative thereof.
35. A fuel composition according to claim 4 characterised in that the fatty acid is oleic acid or a derivative thereof.
36. A fuel composition according to claim 1 characterised in that the composition comprises 25% v/v of the fatty acid ethoxylate or a derivative thereof.
37. A fuel composition according to claim 1 characterised in that the composition comprises 50% v/v of the alcohol ethoxylate.
38. A fuel composition according to claim 1 characterised in that the surfactant additive to fuel ratio is from 0.5:1200 to 50:1000.
39. A method of running an internal combustion engine comprising the use of a fuel according to claim 1.
40. A fuel composition substantially as described with reference to the accompanying examples.
41. The use of oleic acid or a derivative thereof in the manufacture of a fuel composition according to claim 1.
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Cited By (4)

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US20080022584A1 (en) * 2006-07-26 2008-01-31 Mark Schomann Alternative organic fuel formulations including vegetable oil
US20090235574A1 (en) * 2005-03-11 2009-09-24 Earle Martyn J Production of Bio-Diesel
US20090293344A1 (en) * 2008-05-30 2009-12-03 Baker Hughes Incorporated Process for Removing Water and Water Soluble Contaminants From Biofuels
US20090300975A1 (en) * 2008-06-06 2009-12-10 Baker Hughes Incorporated Process for Clarifying Biofuels

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US6017369A (en) * 1998-11-23 2000-01-25 Pure Energy Corporation Diesel fuel composition

Patent Citations (2)

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Publication number Priority date Publication date Assignee Title
US5393791A (en) * 1990-07-19 1995-02-28 Helena Chemical Company Homogeneous, essentially nonaqueous adjuvant compositions with buffering capability
US6017369A (en) * 1998-11-23 2000-01-25 Pure Energy Corporation Diesel fuel composition

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090235574A1 (en) * 2005-03-11 2009-09-24 Earle Martyn J Production of Bio-Diesel
US20080022584A1 (en) * 2006-07-26 2008-01-31 Mark Schomann Alternative organic fuel formulations including vegetable oil
US7901469B2 (en) 2006-07-26 2011-03-08 Alternative Fuels Group Inc. Alternative organic fuel formulations including vegetable oil
US20090293344A1 (en) * 2008-05-30 2009-12-03 Baker Hughes Incorporated Process for Removing Water and Water Soluble Contaminants From Biofuels
US20090300975A1 (en) * 2008-06-06 2009-12-10 Baker Hughes Incorporated Process for Clarifying Biofuels
US9127226B2 (en) 2008-06-06 2015-09-08 Baker Hughes Incorporated Process for clarifying biofuels
US9725668B2 (en) 2008-06-06 2017-08-08 Baker Hughes Incorporated Process for clarifying biofuels

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