US20060123695A1 - Fuel for motor vehicles - Google Patents

Fuel for motor vehicles Download PDF

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Publication number
US20060123695A1
US20060123695A1 US10/551,552 US55155204A US2006123695A1 US 20060123695 A1 US20060123695 A1 US 20060123695A1 US 55155204 A US55155204 A US 55155204A US 2006123695 A1 US2006123695 A1 US 2006123695A1
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US
United States
Prior art keywords
fuel
motor vehicles
vehicles according
previous
emulsion
Prior art date
Legal status (The legal status 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 status listed.)
Abandoned
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US10/551,552
Inventor
Luigi D'Elia
Pietro Scorletti
Riccardo Rausa
Guido Rivolta
Alberto De Amicis
Tiziano Ambrosini
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Eni Tecnologie SpA
Eni SpA
Pirelli and C Ambiente Eco Technology SpA
Original Assignee
Eni SpA
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Assigned to ENITECHNOLOGIE S.P.A., PIRELLI & C. AMBIENTE TECNOLOGIE S.P.A., ENI S.P.A. reassignment ENITECHNOLOGIE S.P.A. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: AMBROSINI, TIZIANO, DE AMICIS, ALBERTO, D'ELIA, LUIGI, RAUSA, RICCARDO, RIVOLTA, GUIDO, SCORLETTI, PIETRO
Assigned to PIRELLI & C. AMBIENTE TECNOLOGIE S.P.A., ENITECNOLOGIE S.P.A., ENI S.P.A. reassignment PIRELLI & C. AMBIENTE TECNOLOGIE S.P.A. CORRECTIVE ASSIGNMENT TO CORRECT THE THIRD ASSIGNE Assignors: AMBROSINI, TIZIANO, DE AMICIS, ALBERTO, D'ELIA, LUIGI, RAUSA, RICCARDO, RIVOLTA, GUIDO, SCORLETTI, PIETRO
Publication of US20060123695A1 publication Critical patent/US20060123695A1/en
Abandoned legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/02Use of additives to fuels or fires for particular purposes for reducing smoke development
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K23/00Use of substances as emulsifying, wetting, dispersing, or foam-producing agents
    • C09K23/16Amines or polyamines
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/32Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
    • C10L1/328Oil emulsions containing water or any other hydrophilic phase
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    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K23/00Use of substances as emulsifying, wetting, dispersing, or foam-producing agents
    • C09K23/22Amides or hydrazides
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K23/00Use of substances as emulsifying, wetting, dispersing, or foam-producing agents
    • C09K23/34Higher-molecular-weight carboxylic acid esters
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1233Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof
    • C10L1/125Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof water
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/185Ethers; Acetals; Ketals; Aldehydes; Ketones
    • C10L1/1857Aldehydes; Ketones
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    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
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    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/195Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/196Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and a carboxyl group or salts, anhydrides or esters thereof homo- or copolymers of compounds having one or more unsaturated aliphatic radicals each having one carbon bond to carbon double bond, and at least one being terminated by a carboxyl radical or of salts, anhydrides or esters thereof
    • C10L1/1963Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and a carboxyl group or salts, anhydrides or esters thereof homo- or copolymers of compounds having one or more unsaturated aliphatic radicals each having one carbon bond to carbon double bond, and at least one being terminated by a carboxyl radical or of salts, anhydrides or esters thereof mono-carboxylic
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/195Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/196Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and a carboxyl group or salts, anhydrides or esters thereof homo- or copolymers of compounds having one or more unsaturated aliphatic radicals each having one carbon bond to carbon double bond, and at least one being terminated by a carboxyl radical or of salts, anhydrides or esters thereof
    • C10L1/1966Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and a carboxyl group or salts, anhydrides or esters thereof homo- or copolymers of compounds having one or more unsaturated aliphatic radicals each having one carbon bond to carbon double bond, and at least one being terminated by a carboxyl radical or of salts, anhydrides or esters thereof poly-carboxylic
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    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/195Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/197Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and an acyloxy group of a saturated carboxylic or carbonic acid
    • C10L1/1973Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and an acyloxy group of a saturated carboxylic or carbonic acid mono-carboxylic
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/198Macromolecular 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
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    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/198Macromolecular 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
    • C10L1/1985Macromolecular 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
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/221Organic compounds containing nitrogen compounds of uncertain formula; reaction products where mixtures of compounds are obtained
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    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/222Organic 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
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    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/23Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites
    • C10L1/231Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites nitro compounds; nitrates; nitrites
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    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/232Organic compounds containing nitrogen containing nitrogen in a heterocyclic ring
    • C10L1/233Organic compounds containing nitrogen containing nitrogen in a heterocyclic ring containing nitrogen and oxygen in the ring, e.g. oxazoles
    • C10L1/2335Organic compounds containing nitrogen containing nitrogen in a heterocyclic ring containing nitrogen and oxygen in the ring, e.g. oxazoles morpholino, and derivatives thereof
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    • C10L1/00Liquid carbonaceous fuels
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    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/236Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derivatives thereof
    • C10L1/2364Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derivatives thereof homo- or copolymers derived from unsaturated compounds containing amide and/or imide groups
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    • C10L1/234Macromolecular compounds
    • C10L1/238Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
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    • C10L1/00Liquid carbonaceous fuels
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    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2443Organic compounds containing sulfur, selenium and/or tellurium heterocyclic compounds
    • C10L1/2456Organic compounds containing sulfur, selenium and/or tellurium heterocyclic compounds sulfur with oxygen and/or nitrogen in the ring, e.g. thiazoles

Definitions

  • the present invention relates to a fuel for motor vehicles.
  • the present invention relates to a fuel for motor vehicles which comprises an emulsion between water and a liquid hydrocarbon.
  • the present invention relates to a fuel for diesel engines with a low emission of pollutants which comprises a high stability emulsion of water in gas oil.
  • Cavitation is the process which occurs when the pressure exerted on the fluid in a particular point is lower than the vapor pressure of the fluid itself (vaporous cavitation). In that point, the liquid vaporizes locally and forms cavities. These cavities, which can flow through the circuit carried by the fluid, subsequently come into contact with higher pressure regions and collapse. The resulting implosion can be extremely violent and can cause vibrations, noise and damage to the materials forming the circuit.
  • a phenomenon very similar to cavitation is generated by gases dissolved in the fluid (gaseous cavitation). If the pressure exerted on the liquid in a particular point is lower than the saturation pressure, the gas abandons the liquid forming bubbles. The bubbles initially increase in volume, but are then re-dissolved in the higher pressure areas of the circuit. Bubbles, however, may already be present in the fluid, for example, air dissolved in the fuel contained in a tank. As, in practice, it is extremely difficult to distinguish between these two cavitation processes, reference will be made herein, when speaking about cavitation, to both. Further details on cavitation can be found in SAE 982036 “Hydraulic system cavitation: A review” or in SAE 1999-01-2857 “Hydraulic system cavitation: part II—A Review of hardware design—related effect”.
  • the Applicants consequently considered the problem of reducing the risk of activating erosion phenomena as a result of cavitation in internal combustion engines fed with fuels in the form of aqueous emulsion, without jeopardizing the stability of the emulsion itself and without resorting to mechanical means.
  • An object of the present invention therefore relates to a fuel for motor vehicles comprising an emulsion between water and a liquid hydrocarbon, and an anti-cavitation additive comprising a copolymer including 20-80% in moles, preferably 35-70% in moles, of units containing at least one carboxylic group and 80-20% in moles, preferably 65-30% in moles, of units deriving from at least one monomer having an ethylene unsaturation, and wherein at least 20% in moles of the carboxylic groups, preferably 30-90% in moles, is in the form of at least one derivative selected from carboxylate salt, ester, amide and imide.
  • the copolymer according to the present invention preferably has an average molecular weight Mw ranging from 700 to 3000.
  • the carboxylic groups can be partially or totally salified by means of a neutralization reaction carried out with an inorganic or organic base.
  • bases suitable for the reaction are hydroxides of alkaline or alkaline earth metals, ammonium hydroxide or quaternary ammonium hydroxides, sodium and/or potassium carbonates and bicarbonates, C 1 -C 30 aliphatic alkylamines.
  • the bases preferably used are sodium or ammonium hydroxide.
  • the carboxylic groups can be partially or totally esterified using an alcohol or polyol with a low number of carbon atoms, selected, for example from: C 1 -C 5 alcohols, such as methanol, ethanol, (iso)propanol, (iso)butanol, ethylene glycol, glycerin and diethylene glycol.
  • an alcohol or polyol with a low number of carbon atoms selected, for example from: C 1 -C 5 alcohols, such as methanol, ethanol, (iso)propanol, (iso)butanol, ethylene glycol, glycerin and diethylene glycol.
  • the carboxylic groups can also be partially or totally transformed into amide or imide groups, by means of thermal treatment, with a primary or secondary aliphatic amine with a low number of carbon atoms, selected, for example, from C 1 -C 8 alkyl or dialkyl amines, such as ethyl amine, propyl amine, butyl amine, pentyl amine, hexyl amine, dimethyl amine, diethyl amine, dipropyl amine, dibutyl amine, etc.
  • a primary or secondary aliphatic amine with a low number of carbon atoms selected, for example, from C 1 -C 8 alkyl or dialkyl amines, such as ethyl amine, propyl amine, butyl amine, pentyl amine, hexyl amine, dimethyl amine, diethyl amine, dipropyl amine, dibutyl amine, etc.
  • Preferred monomers containing at least one carboxylic group according to the present invention are:
  • Any monomers having an ethylene unsaturation capable of copolymerizing with acids having an ethylene unsaturation can be used in the preparation of the anti-cavitation agent according to the present invention.
  • Typical examples include: C 2 -C 12 ⁇ -olefins, such as ethylene, propylene, 1-butene, 1-pentene, 1-hexene, etc.; C 1 -C 6 alkyl esters of (meth)acrylic acid such as methyl (meth)acrylate, ethyl (meth)acrylate, butyl (meth)acrylate; vinyl ethers and vinyl esters.
  • vinyl ethers are: vinyl methyl ether, vinyl ethyl ether, vinyl n-propyl ether, vinyl isopropyl ether, vinyl n-butyl ether, vinyl isobutyl ether, vinyl t-butyl ether, vinyl hexyl ether.
  • vinyl esters are: vinyl formiate, vinyl acetate, vinyl propionate, vinyl butyrate and vinyl pivalate.
  • a further object of the present invention relates to a process for feeding an internal combustion engine, which comprises: feeding a fuel into a combustion chamber of said engine; igniting said fuel in said combustion chamber, wherein said fuel comprises an emulsion between water and a liquid hydrocarbon, and an anti-cavitation additive as described above.
  • the preferred internal combustion engine is a diesel cycle engine.
  • the liquid hydrocarbon of the fuel for motor vehicles, object of the present invention is generally a derivative from oil distillation and essentially consists of mixtures of aliphatic, naphthenic, olefinic and/or aromatic hydrocarbons.
  • the liquid hydrocarbon preferably has a viscosity at 40° C. ranging from 1 to 5.3 cSt and a density at 15° C. ranging from 0.75 to 1.1 kg/dm 3 .
  • Preferred liquid hydrocarbons according to the present invention are gas oils for diesel engines, kerosenes and aviation fuels.
  • the quantity of water present in the emulsion generally ranges from 2 to 40% by weight, preferably from 3 to 20% by weight, even more preferably from 4 to 10% by weight, with respect to the total weight of the emulsion. Any type of water can be used, both for industrial and domestic use. Demineralized or deionized water is preferably used, however, to avoid the formation of crusts on the internal surface of the combustion chamber or in the fuel flow areas, for example on the injectors.
  • the type of emulsion which characterizes the fuel for motor vehicles, object of the present invention is generally of the water-in-oil type, in which the particles of water are dispersed in the continuous hydrocarbon phase.
  • the use of at least one emulsifying agent is preferred, whose concentration depends on the quantity of water to be emulsified and the type of hydrocarbon used. Said concentration generally ranges from 0.1 to 10% by weight with respect to the total, preferably from 0.5 to 5%.
  • the emulsifying agent, or combination of emulsifying agents preferably has an HLB (Hydrophilic-Lipophilic Balance) value ranging from 2 to 10, preferably from 3 to 8.
  • HLB Hydrophilic-Lipophilic Balance
  • Emulsifying agents suitable for the purpose can be selected, for example, from:
  • Emulsifying agents suitable for the purpose can also be selected from: alkanol amides, alkylaryl sulfonates, amino oxides, polyoxy-alkylenes (including ethylene oxide-propylene oxide block copolymers), ethoxylated or propoxylated/ethoxylated alcohols, carboxylates of ethoxylated or propoxylated/ethoxylated alcohols, ethoxylated or propoxylated/ethoxylated alkyl phenols, ethoxylated or propoxylated/ethoxylated amines and amides, ethoxylated or propoxylated/ethoxylated fatty acids, esters of fatty acids, ethoxylated or propoxylated/ethoxylated esters of fatty acids, esters of polyalcohols (preferably of ethylene glycol or glycerol), imidazoline derivatives, lecithins and derivatives, lignins and derivatives,
  • a particularly preferred emulsifying agent is selected from the products of group (a) listed above.
  • the polyolefinic oligomer preferably has an average molecular weight ranging from 300 to 10,000, more preferably from 500 to 5,000, and is obtained by the homopolymerization or copolymerization of one or more olefins having from 2 to 16 carbon atoms.
  • the preferred polyolefinic oligomer is that containing at least 80% in moles of units deriving from isobutene, the remaining percentage consisting of units deriving from linear butene.
  • the polyoxy-alkylene comprises oxyalkylene units, each containing two or three carbon atoms.
  • the polyoxy-alkylene is preferably polyoxy-ethylene containing from 2 to 40, preferably from 5 to 20, oxy-ethylene units having the formula —CH 2 CH 2 O—.
  • the long-chain alkyl group bound to the polyoxy-alkylene preferably derives from a C 8 -C 24 fatty acid or fatty alcohol, optionally containing one or more ethylene unsaturations.
  • fatty acids are: stearic acid, palmitic acid, myristic acid, lauric acid, oleic acid, etc.
  • fatty alcohols are: octyl alcohol, decyl alcohol, lauryl alcohol, myristic alcohol, cetyl alcohol, oleic alcohol, etc.
  • the emulsion thus obtained has a high stability over a period of time, generally for over three months, without forming continuous aqueous phases inside the storage tank which can produce stratifications inside the hydrocarbon phase.
  • This stability remains substantially unvaried also with temperature conditions ranging from ⁇ 20 to 50° C.
  • the fuel for motor vehicles, object of the present invention can contain other additives selected from: cetane number enhancers, corrosion inhibitors, lubricants, biocides, antifoam agents and anti-freeze agents.
  • the cetane number enhancers are products which tend to improve the detonating power of the fuel and are generally selected from nitrates, nitrites and peroxides of an organic or inorganic nature, soluble in aqueous phase or, preferably, in the hydrocarbon phase.
  • Organic nitrates such as alkyl nitrates or cyclo-alkyls containing from 1 to 10 carbon atoms, are particularly preferred.
  • biocides are selected from products known in the art, having this function such as, for example, derivatives of morpholine, derivatives of isothiazolin-3-one, tris(hydroxymethyl)-nitro methane, formaldehyde and their mixtures.
  • the fuel, object of the present invention preferably also contains at least one anti-freeze additive to prevent the solidification of the water particles suspended in the hydrocarbon phase, when the environmental temperature drops well below zero.
  • anti-freeze additives are alcohols such as methanol, ethanol, isopropanol and glycols such as ethylene glycol.
  • the anti-freeze additive is generally added in a quantity ranging from 0.5 to 8% by weight, with respect to the total, preferably from 1 to 4%.
  • the fuel for motor vehicles, object of the present invention can be prepared by mixing the components in dynamic emulsifying devices, through which the formation of the emulsion is effected by means of a mechanical action exerted by mobile parts, or by means of static devices, through which the emulsion components are passed at a high velocity or, alternatively, by means of a combination of the two types of devices.
  • the emulsion can be formed by feeding the aqueous phase and hydrocarbon phase, optionally premixed, to the dynamic and/or static devices.
  • the additives can be pre-dissolved in the two phases or added separately, together with the water and hydrocarbon phase.

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Abstract

Fuel for motor vehicles comprising an emulsion between water and a liquid hydrocarbon, and an anti-cavitation additive comprising a copolymer including 20-80% in moles, preferably 35-70% in moles, of units containing at least one carboxylic group and 80-20% in moles, preferably 65-30% in moles, of units deriving from at least one monomer having an ethylene unsaturation, and wherein at least 20% in moles of the carboxylic groups, preferably 30-90% in moles, is in the form of at least one derivative selected from carboxylate salt, ester, amide and imide.

Description

  • The present invention relates to a fuel for motor vehicles.
  • More specifically, the present invention relates to a fuel for motor vehicles which comprises an emulsion between water and a liquid hydrocarbon.
  • Even more specifically, the present invention relates to a fuel for diesel engines with a low emission of pollutants which comprises a high stability emulsion of water in gas oil.
  • The new anti-pollution regulations which have come into force in Italy and the main European countries in the last few years, have compelled motor vehicle manufacturers to significantly update internal combustion engines and fuel producers to offer fuels with a low environmental impact.
  • The introduction of so-called green gasoline and the use of catalytic converters have led to the necessity of changing the feeding control system of Otto cycle engines, which has passed from the carburetor method to the electronic injection method.
  • For similar reasons, in particular for reducing emissions of particulate and NOx, new Diesel cycle engines have been proposed, in which up-to-date electronic control systems have been introduced, which are capable of effecting the direct injection of fuel into the combustion chamber with pressures of over 1300 bar.
  • Furthermore, new ecological gas oils in emulsion form have been recently introduced onto the market, comprising a aqueous phase finely dispersed in the form of droplets in the hydrocarbon phase, stabilized by suitable emulsifying agents (see for example patent applications WO 97/34969, WO 00/15740 and WO 01/51593). The addition of controlled quantities of water to a fuel, in fact, significantly reduces the production of polluting agents. It is believed that this effect is the result of various phenomena activated by the presence of water in the combustion zones. Water, for example, by lowering the peak combustion temperature, reduces the emission of nitrogen oxides (NOx), whose formation is favoured by high temperatures. The instantaneous vaporization of water also favours a better dispersion of the hydrocarbon in the combustion chamber, thus greatly reducing the formation of particulate. These phenomena occur without jeopardizing the combustion process performance.
  • The use of injectors, both in gasoline and Diesel engines, and consequently very high feeding pressures, in particular for the latter, has created the necessity of developing and using new materials capable of sustaining, under typical internal combustion engine conditions, the stress imposed by new fuel feeding systems. In spite of this, the use of high pressures has led to erosion phenomena as a result of cavitation which can also be critical for the most advanced materials currently used in the transport industry. In particular, it has been verified that cavitation phenomena can arise in feeding devices as a result of brusque changes in the direction of the fluid on the feeding pipes of the pressurization pump or in the secondary pipes which lead to the injectors or on the tips of the injectors themselves.
  • Cavitation is the process which occurs when the pressure exerted on the fluid in a particular point is lower than the vapor pressure of the fluid itself (vaporous cavitation). In that point, the liquid vaporizes locally and forms cavities. These cavities, which can flow through the circuit carried by the fluid, subsequently come into contact with higher pressure regions and collapse. The resulting implosion can be extremely violent and can cause vibrations, noise and damage to the materials forming the circuit.
  • A phenomenon very similar to cavitation is generated by gases dissolved in the fluid (gaseous cavitation). If the pressure exerted on the liquid in a particular point is lower than the saturation pressure, the gas abandons the liquid forming bubbles. The bubbles initially increase in volume, but are then re-dissolved in the higher pressure areas of the circuit. Bubbles, however, may already be present in the fluid, for example, air dissolved in the fuel contained in a tank. As, in practice, it is extremely difficult to distinguish between these two cavitation processes, reference will be made herein, when speaking about cavitation, to both. Further details on cavitation can be found in SAE 982036 “Hydraulic system cavitation: A review” or in SAE 1999-01-2857 “Hydraulic system cavitation: part II—A Review of hardware design—related effect”.
  • At present, attempts have been made to solve the problem of cavitation induced in fuels for motor vehicles, mechanically, as described, for example in U.S. Pat. Nos. 6,045,162 and 6,070,618.
  • The Applicants believe that the cavitation phenomena described above can become particularly significant with the use of fuels in the form of aqueous emulsion. These fuels, in fact, have a heterogeneous structure in which the conditions of the aqueous phase, that has a surface tension higher than that of the hydrocarbon, are more favourable for forming cavities.
  • The Applicants consequently considered the problem of reducing the risk of activating erosion phenomena as a result of cavitation in internal combustion engines fed with fuels in the form of aqueous emulsion, without jeopardizing the stability of the emulsion itself and without resorting to mechanical means.
  • The Applicants have found that the above problem can be solved by adding a polymeric additive containing carboxylic groups and/or groups deriving from carboxylic groups as defined hereunder, to the fuel in the form of an aqueous emulsion.
  • An object of the present invention therefore relates to a fuel for motor vehicles comprising an emulsion between water and a liquid hydrocarbon, and an anti-cavitation additive comprising a copolymer including 20-80% in moles, preferably 35-70% in moles, of units containing at least one carboxylic group and 80-20% in moles, preferably 65-30% in moles, of units deriving from at least one monomer having an ethylene unsaturation, and wherein at least 20% in moles of the carboxylic groups, preferably 30-90% in moles, is in the form of at least one derivative selected from carboxylate salt, ester, amide and imide.
  • The copolymer according to the present invention preferably has an average molecular weight Mw ranging from 700 to 3000.
  • The carboxylic groups can be partially or totally salified by means of a neutralization reaction carried out with an inorganic or organic base.
  • Examples of bases suitable for the reaction are hydroxides of alkaline or alkaline earth metals, ammonium hydroxide or quaternary ammonium hydroxides, sodium and/or potassium carbonates and bicarbonates, C1-C30 aliphatic alkylamines. The bases preferably used are sodium or ammonium hydroxide.
  • Alternatively, the carboxylic groups can be partially or totally esterified using an alcohol or polyol with a low number of carbon atoms, selected, for example from: C1-C5 alcohols, such as methanol, ethanol, (iso)propanol, (iso)butanol, ethylene glycol, glycerin and diethylene glycol.
  • The carboxylic groups can also be partially or totally transformed into amide or imide groups, by means of thermal treatment, with a primary or secondary aliphatic amine with a low number of carbon atoms, selected, for example, from C1-C8 alkyl or dialkyl amines, such as ethyl amine, propyl amine, butyl amine, pentyl amine, hexyl amine, dimethyl amine, diethyl amine, dipropyl amine, dibutyl amine, etc.
  • Preferred monomers containing at least one carboxylic group according to the present invention are:
  • (a) C3-C10 aliphatic monocarboxylic acids having an ethylene unsaturation, for example: acrylic acid, methacrylic acid, vinyl acetic acid, crotonic acid, allyl acetic acid, etc.
  • (b) C4-C10 aliphatic dicarboxylic acids having an ethylene unsaturation, for example: maleic acid, itaconic acid, citraconic acid, fumaric acid, methylene malonic acid, and the like, and their anhydrides.
  • Any monomers having an ethylene unsaturation capable of copolymerizing with acids having an ethylene unsaturation, can be used in the preparation of the anti-cavitation agent according to the present invention. Typical examples include: C2-C12 α-olefins, such as ethylene, propylene, 1-butene, 1-pentene, 1-hexene, etc.; C1-C6 alkyl esters of (meth)acrylic acid such as methyl (meth)acrylate, ethyl (meth)acrylate, butyl (meth)acrylate; vinyl ethers and vinyl esters.
  • Examples of vinyl ethers are: vinyl methyl ether, vinyl ethyl ether, vinyl n-propyl ether, vinyl isopropyl ether, vinyl n-butyl ether, vinyl isobutyl ether, vinyl t-butyl ether, vinyl hexyl ether.
  • Examples of vinyl esters are: vinyl formiate, vinyl acetate, vinyl propionate, vinyl butyrate and vinyl pivalate.
  • A further object of the present invention relates to a process for feeding an internal combustion engine, which comprises: feeding a fuel into a combustion chamber of said engine; igniting said fuel in said combustion chamber, wherein said fuel comprises an emulsion between water and a liquid hydrocarbon, and an anti-cavitation additive as described above. The preferred internal combustion engine is a diesel cycle engine.
  • The liquid hydrocarbon of the fuel for motor vehicles, object of the present invention, is generally a derivative from oil distillation and essentially consists of mixtures of aliphatic, naphthenic, olefinic and/or aromatic hydrocarbons. The liquid hydrocarbon preferably has a viscosity at 40° C. ranging from 1 to 5.3 cSt and a density at 15° C. ranging from 0.75 to 1.1 kg/dm3. Preferred liquid hydrocarbons according to the present invention are gas oils for diesel engines, kerosenes and aviation fuels.
  • The quantity of water present in the emulsion generally ranges from 2 to 40% by weight, preferably from 3 to 20% by weight, even more preferably from 4 to 10% by weight, with respect to the total weight of the emulsion. Any type of water can be used, both for industrial and domestic use. Demineralized or deionized water is preferably used, however, to avoid the formation of crusts on the internal surface of the combustion chamber or in the fuel flow areas, for example on the injectors.
  • The type of emulsion which characterizes the fuel for motor vehicles, object of the present invention, is generally of the water-in-oil type, in which the particles of water are dispersed in the continuous hydrocarbon phase.
  • In order to obtain emulsions which are stable over a period of time and with temperature variations, the use of at least one emulsifying agent is preferred, whose concentration depends on the quantity of water to be emulsified and the type of hydrocarbon used. Said concentration generally ranges from 0.1 to 10% by weight with respect to the total, preferably from 0.5 to 5%.
  • The emulsifying agent, or combination of emulsifying agents, preferably has an HLB (Hydrophilic-Lipophilic Balance) value ranging from 2 to 10, preferably from 3 to 8.
  • Emulsifying agents suitable for the purpose can be selected, for example, from:
  • (a) products obtained by the reaction of (a1) a polyolefinic oligomer functionalized with at least one group deriving from a dicarboxylic acid, or one of its derivatives, with (a2) a polyoxy-alkylene comprising linear oxy-alkylene units, said polyoxy-alkylene being bound to a long-chain alkyl group optionally containing at least one ethylene unsaturation;
  • (b) products obtained by the reaction of (b1) a carboxylic acylating agent containing a hydrocarbon chain having from 50 to 500 carbon atoms, with (b2) ammonia or an amine.
  • Emulsifying agents suitable for the purpose can also be selected from: alkanol amides, alkylaryl sulfonates, amino oxides, polyoxy-alkylenes (including ethylene oxide-propylene oxide block copolymers), ethoxylated or propoxylated/ethoxylated alcohols, carboxylates of ethoxylated or propoxylated/ethoxylated alcohols, ethoxylated or propoxylated/ethoxylated alkyl phenols, ethoxylated or propoxylated/ethoxylated amines and amides, ethoxylated or propoxylated/ethoxylated fatty acids, esters of fatty acids, ethoxylated or propoxylated/ethoxylated esters of fatty acids, esters of polyalcohols (preferably of ethylene glycol or glycerol), imidazoline derivatives, lecithins and derivatives, lignins and derivatives, mono-glycerides and derivatives, alkyl sulfonates, esters of phosphoric acid and derivatives, sorbitan derivatives, esters of sucrose and derivatives, or their mixtures.
  • Further details on emulsifying agents which can be used in the fuels according to the present invention are described in EP-A-475,620, EP-A-630,398, WO 97/34969, EP-A812,615, WO 92/19701, WO 93/07238, WO 00/15740, whose contents are incorporated herein as reference.
  • A particularly preferred emulsifying agent is selected from the products of group (a) listed above.
  • The polyolefinic oligomer preferably has an average molecular weight ranging from 300 to 10,000, more preferably from 500 to 5,000, and is obtained by the homopolymerization or copolymerization of one or more olefins having from 2 to 16 carbon atoms. The preferred polyolefinic oligomer is that containing at least 80% in moles of units deriving from isobutene, the remaining percentage consisting of units deriving from linear butene.
  • The polyoxy-alkylene comprises oxyalkylene units, each containing two or three carbon atoms. The polyoxy-alkylene is preferably polyoxy-ethylene containing from 2 to 40, preferably from 5 to 20, oxy-ethylene units having the formula —CH2CH2O—.
  • The long-chain alkyl group bound to the polyoxy-alkylene preferably derives from a C8-C24 fatty acid or fatty alcohol, optionally containing one or more ethylene unsaturations. Examples of fatty acids are: stearic acid, palmitic acid, myristic acid, lauric acid, oleic acid, etc. Examples of fatty alcohols are: octyl alcohol, decyl alcohol, lauryl alcohol, myristic alcohol, cetyl alcohol, oleic alcohol, etc.
  • More precise details on said emulsifying agent are provided in international patent application WO 01/51593, whose contents are incorporated herein as reference.
  • The emulsion thus obtained has a high stability over a period of time, generally for over three months, without forming continuous aqueous phases inside the storage tank which can produce stratifications inside the hydrocarbon phase. This stability remains substantially unvaried also with temperature conditions ranging from −20 to 50° C.
  • The stability of the emulsion, moreover, is not substantially jeopardized by the anti-cavitation agent. The latter is soluble in the emulsion and is present in concentrations ranging from 30 ppm to 3% by weight, preferably from 50 ppm to 1.5% by weight, with respect to the overall weight of the emulsion.
  • The fuel for motor vehicles, object of the present invention, can contain other additives selected from: cetane number enhancers, corrosion inhibitors, lubricants, biocides, antifoam agents and anti-freeze agents. The cetane number enhancers, for example, are products which tend to improve the detonating power of the fuel and are generally selected from nitrates, nitrites and peroxides of an organic or inorganic nature, soluble in aqueous phase or, preferably, in the hydrocarbon phase. Organic nitrates, such as alkyl nitrates or cyclo-alkyls containing from 1 to 10 carbon atoms, are particularly preferred.
  • The biocides are selected from products known in the art, having this function such as, for example, derivatives of morpholine, derivatives of isothiazolin-3-one, tris(hydroxymethyl)-nitro methane, formaldehyde and their mixtures.
  • Finally, the fuel, object of the present invention, preferably also contains at least one anti-freeze additive to prevent the solidification of the water particles suspended in the hydrocarbon phase, when the environmental temperature drops well below zero. Examples of anti-freeze additives are alcohols such as methanol, ethanol, isopropanol and glycols such as ethylene glycol. The anti-freeze additive is generally added in a quantity ranging from 0.5 to 8% by weight, with respect to the total, preferably from 1 to 4%.
  • The fuel for motor vehicles, object of the present invention, can be prepared by mixing the components in dynamic emulsifying devices, through which the formation of the emulsion is effected by means of a mechanical action exerted by mobile parts, or by means of static devices, through which the emulsion components are passed at a high velocity or, alternatively, by means of a combination of the two types of devices. The emulsion can be formed by feeding the aqueous phase and hydrocarbon phase, optionally premixed, to the dynamic and/or static devices. The additives can be pre-dissolved in the two phases or added separately, together with the water and hydrocarbon phase.

Claims (18)

1. A fuel for motor vehicles comprising an emulsion between water and a liquid hydrocarbon, and an anti-cavitation additive, including a copolymer comprising 20-80% in moles of units containing at least one carboxylic group and 80-20% in moles of units deriving from at least one monomer having an ethylene unsaturation, and wherein at least 20% in moles of the carboxylic groups is in the form of at least one derivative selected from carboxylate salt, ester, amide and imide.
2. The fuel for motor vehicles according to claim 1, wherein the copolymer has an average molecular weight Mw ranging from 700 to 3000.
3. The fuel for motor vehicles according to claim 1 or 2, wherein the carboxylic groups present in the copolymer are partially or totally salified by means of a neutralization reaction carried out with an inorganic or organic base.
4. The fuel for motor vehicles according to claim 3, wherein the base is selected from: hydroxides of alkaline or alkaline earth metals, ammonium hydroxide or quaternary ammonium hydroxides, sodium and/or potassium carbonates and bicarbonates, C1-C30 aliphatic alkyl amines.
5. The fuel for motor vehicles according to claim 1 or 2, wherein the carboxylic groups present in the copolymer are partially or totally esterified by means of an alcohol or a polyol with a low number of carbon atoms.
6. The fuel for motor vehicles according to claim 1 or 2, wherein the carboxylic acid groups present in the copolymer are partially or totally transformed into amide or imide groups by means of thermal treatment in the presence of a primary or secondary aliphatic amine with a low number of carbon atoms.
7. The fuel for motor vehicles according to any of the previous claims, wherein the units containing at least one carboxylic group derive from a C3-C10 aliphatic monocarboxylic acid having an ethylene unsaturation, or from a C4-C10 aliphatic dicarboxylic acid having an ethylene unsaturation.
8. The fuel for motor vehicles according to any of the previous claims, wherein the monomer having an ethylene unsaturation is selected from: C2-C12 α-olefins, C1-C6 alkyl esters of (meth)acrylic acid, vinyl ethers and vinyl esters.
9. The fuel for motor vehicles according to any of the previous claims, wherein the liquid hydrocarbon has a viscosity at 40° C. ranging from 1 to 5.3 cSt and a density at 15° C. ranging from 0.75 to 1.1 kg/dm3.
10. The fuel for motor vehicles according to any of the previous claims, wherein the water is present in a quantity ranging from 2 to 40% by weight, with respect to the total.
11. The fuel for motor vehicles according to any of the previous claims, wherein the emulsion is of the water-in-oil type.
12. The fuel for motor vehicles according to claim 11, wherein the emulsion comprises at least one emulsifying agent whose concentration ranges from 0.1 to 10% by weight with respect to the total.
13. The fuel for motor vehicles according to any of the previous claims, wherein said at least one emulsifying agent has an HLB (Hydrophilic-Lipophilic Balance) value ranging from 2 to 10.
14. The fuel for motor vehicles according to claim 13, wherein said at least one emulsifying agent has an HLB (Hydrophilic-Lipophilic Balance) value ranging from 3 to 8.
15. The fuel for motor vehicles according to any of the previous claims, wherein said at least one emulsifying agent is a product obtained by the reaction of: (a1) a polyolefinic oligomer functionalized with at least one group deriving from a dicarboxylic acid, or one of its derivatives; with (a2) a polyoxy-alkylene comprising linear oxy-alkylene units, said polyoxy-alkylene being bound to a long-chain alkyl group optionally containing at least one ethylene unsaturation.
16. The fuel for motor vehicles according to any of the claims from 1 to 14, wherein said at least one emulsifying agent is a product obtained by the reaction of (b1) a carboxylic acylating agent containing a hydrocarbon chain having from 50 to 500 carbon atoms, with (b2) ammonia or an amine.
17. A process for feeding an internal combustion engine which comprises: feeding a fuel to a combustion chamber of said engine; igniting said fuel in said combustion chamber, wherein said fuel comprises an emulsion between water and a liquid hydrocarbon, and an anti-cavitation additive according to any of the claims from 1 to 16.
18. The process according to claim 17, wherein the internal combustion engine is a diesel cycle engine.
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US9493709B2 (en) 2011-03-29 2016-11-15 Fuelina Technologies, Llc Hybrid fuel and method of making the same
US10308885B2 (en) 2014-12-03 2019-06-04 Drexel University Direct incorporation of natural gas into hydrocarbon liquid fuels

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