WO2001062876A1 - Compositions - Google Patents

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Publication number
WO2001062876A1
WO2001062876A1 PCT/GB2001/000749 GB0100749W WO0162876A1 WO 2001062876 A1 WO2001062876 A1 WO 2001062876A1 GB 0100749 W GB0100749 W GB 0100749W WO 0162876 A1 WO0162876 A1 WO 0162876A1
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WO
WIPO (PCT)
Prior art keywords
fuel composition
composition according
alcohol
fatty acid
fuel
Prior art date
Application number
PCT/GB2001/000749
Other languages
French (fr)
Inventor
Alan Rae
Original Assignee
Aae Technologies International Limited
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Aae Technologies International Limited filed Critical Aae Technologies International Limited
Priority to AU2001235764A priority Critical patent/AU2001235764A1/en
Priority to EP01907896A priority patent/EP1257616A1/en
Priority to BR0108703-7A priority patent/BR0108703A/en
Priority to MXPA02008272A priority patent/MXPA02008272A/en
Priority to PL01357388A priority patent/PL357388A1/en
Priority to CA002400944A priority patent/CA2400944A1/en
Publication of WO2001062876A1 publication Critical patent/WO2001062876A1/en

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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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/143—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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/02—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • C10L1/026—Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for compression ignition
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00—Use of additives to fuels or fires for particular purposes
    • C10L10/02—Use of additives to fuels or fires for particular purposes for reducing smoke development
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00—Use of additives to fuels or fires for particular purposes
    • C10L10/06—Use of additives to fuels or fires for particular purposes for facilitating soot removal
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/185—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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/19—Esters ester radical containing compounds; ester ethers; carbonic acid 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/19—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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/192—Macromolecular compounds
    • C10L1/198—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
    • C10L1/1985—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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/22—Organic compounds containing nitrogen
    • C10L1/222—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
    • C10L1/224—Amides; Imides carboxylic acid amides, imides
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/10—Biofuels, e.g. bio-diesel

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 fuel has been considered as an alternative to petroleum based diesel.
  • 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.
  • 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%o 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] 8 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 $ 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 Cj j 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 18j oleic acid or a derivative thereof, such as an oleate ester, e.g. an alkyl Cj to Q 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 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.
  • HLB hydrophilic-lipophilic balance
  • HLB mol. wt of hydrophilic chain x 20 total mol. wt
  • 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.

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

COMPOSITIONS
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.
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.
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.
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. We have now surprisingly found a fuel composition which overcomes or mitigates the problems of prior art fuels.
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.
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%o v/v.
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.
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 C5 to C20, preferably C8 to C18, more preferably C10 to C18. The most preferred diethanolamide is a C]8 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;
Acid + alkanolamine = alkanolamide + water Plant or animal oil (triglyceride) + alkanolamine = alkanolamide+glycerol Methyl ester + alkanolamine = alkanolamide + methanol
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.
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 C5 to C22 alkanol, more preferably C$ 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 Cj j 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 C18j oleic acid or a derivative thereof, such as an oleate ester, e.g. an alkyl Cj to Q 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.
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.
HLB = mol. wt of hydrophilic chain x 20 total mol. wt
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.
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.
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. 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.
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.
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. In the aforementioned ratios the fuel is considered to comprise the sum of any petroleum diesel, biodiesel and alcohol present in the composition.
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 byproducts formed during the combustion of the fuel.

Claims

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 Cg to C\& 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 Cj; 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 C 0 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 Cj4 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%ι 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.
PCT/GB2001/000749 2000-02-26 2001-02-22 Compositions WO2001062876A1 (en)

Priority Applications (6)

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AU2001235764A AU2001235764A1 (en) 2000-02-26 2001-02-22 Compositions
EP01907896A EP1257616A1 (en) 2000-02-26 2001-02-22 Compositions
BR0108703-7A BR0108703A (en) 2000-02-26 2001-02-22 Combustible composition, method of operating an internal combustion engine and using oleic acid or a derivative thereof.
MXPA02008272A MXPA02008272A (en) 2000-02-26 2001-02-22 Compositions.
PL01357388A PL357388A1 (en) 2000-02-26 2001-02-22 Compositions
CA002400944A CA2400944A1 (en) 2000-02-26 2001-02-22 Compositions

Applications Claiming Priority (2)

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GBGB0004518.7A GB0004518D0 (en) 2000-02-26 2000-02-26 Compositions
GB0004518.7 2000-02-26

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CN (1) CN1406269A (en)
AU (1) AU2001235764A1 (en)
BR (1) BR0108703A (en)
CA (1) CA2400944A1 (en)
GB (1) GB0004518D0 (en)
MX (1) MXPA02008272A (en)
PL (1) PL357388A1 (en)
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US7208022B2 (en) 2002-03-14 2007-04-24 The Lubrizol Corporation Ethanol-diesel fuel composition and methods thereof
GB2445355A (en) * 2007-01-05 2008-07-09 Biofuel Systems Group Ltd Fuel and method of production thereof
US8147566B2 (en) 1999-11-23 2012-04-03 Krogh James A Fuel additive, additive-containing fuel compositions and method of manufacture
CN102851006A (en) * 2012-09-30 2013-01-02 中国石油集团西部钻探工程有限公司 Bio-oil lubricant for drilling wells and preparation method of bio-oil lubricant

Families Citing this family (2)

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US7279018B2 (en) 2002-09-06 2007-10-09 Fortum Oyj Fuel composition for a diesel engine
US8022258B2 (en) 2005-07-05 2011-09-20 Neste Oil Oyj Process for the manufacture of diesel range hydrocarbons

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WO1998056878A1 (en) * 1997-06-09 1998-12-17 Donald Murray Craig Additives enabling blending of polar and non-polar fuel components
WO1999020715A1 (en) * 1997-10-20 1999-04-29 Pure Energy Corporation Polymeric fuel additive and method of making the same, and fuel containing the additive
WO1999052994A1 (en) * 1998-04-09 1999-10-21 Coval Technologies Limited Solubilising compositon
WO1999060078A1 (en) * 1998-05-15 1999-11-25 Lundin Investments (Proprietary) Limited A composition for mixing oil and water to form a solution
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GB2217229A (en) * 1988-04-25 1989-10-25 Enersolve Chemical Company Lim Solubilising composition
WO1998017745A1 (en) * 1996-10-18 1998-04-30 Hamelin Holdings Limited Fuel composition
WO1998056878A1 (en) * 1997-06-09 1998-12-17 Donald Murray Craig Additives enabling blending of polar and non-polar fuel components
WO1999020715A1 (en) * 1997-10-20 1999-04-29 Pure Energy Corporation Polymeric fuel additive and method of making the same, and fuel containing the additive
WO1999052994A1 (en) * 1998-04-09 1999-10-21 Coval Technologies Limited Solubilising compositon
WO1999060078A1 (en) * 1998-05-15 1999-11-25 Lundin Investments (Proprietary) Limited A composition for mixing oil and water to form a solution
US6017369A (en) * 1998-11-23 2000-01-25 Pure Energy Corporation Diesel fuel composition

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8147566B2 (en) 1999-11-23 2012-04-03 Krogh James A Fuel additive, additive-containing fuel compositions and method of manufacture
US7208022B2 (en) 2002-03-14 2007-04-24 The Lubrizol Corporation Ethanol-diesel fuel composition and methods thereof
GB2445355A (en) * 2007-01-05 2008-07-09 Biofuel Systems Group Ltd Fuel and method of production thereof
CN102851006A (en) * 2012-09-30 2013-01-02 中国石油集团西部钻探工程有限公司 Bio-oil lubricant for drilling wells and preparation method of bio-oil lubricant

Also Published As

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EP1257616A1 (en) 2002-11-20
BR0108703A (en) 2002-12-10
MXPA02008272A (en) 2004-06-30
CA2400944A1 (en) 2001-08-30
AU2001235764A1 (en) 2001-09-03
PL357388A1 (en) 2004-07-26
CN1406269A (en) 2003-03-26
GB0004518D0 (en) 2000-04-19

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