EP2029703A2 - Additifs de carburant - Google Patents

Additifs de carburant

Info

Publication number
EP2029703A2
EP2029703A2 EP07759620A EP07759620A EP2029703A2 EP 2029703 A2 EP2029703 A2 EP 2029703A2 EP 07759620 A EP07759620 A EP 07759620A EP 07759620 A EP07759620 A EP 07759620A EP 2029703 A2 EP2029703 A2 EP 2029703A2
Authority
EP
European Patent Office
Prior art keywords
fuel
organic solvent
alkali metal
additive
fuel additive
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.)
Withdrawn
Application number
EP07759620A
Other languages
German (de)
English (en)
Inventor
Llc Petrocrystal
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Publication of EP2029703A2 publication Critical patent/EP2029703A2/fr
Withdrawn legal-status Critical Current

Links

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
    • C10L10/00—Use of additives to fuels or fires for particular purposes
    • C10L10/08—Use of additives to fuels or fires for particular purposes for improving lubricity; for reducing wear
    • 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
    • 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
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L10/00—Use of additives to fuels or fires for particular purposes
    • C10L10/04—Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
    • 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
    • C10L10/00—Use of additives to fuels or fires for particular purposes
    • C10L10/12—Use of additives to fuels or fires for particular purposes for improving the cetane number
    • 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
    • C10L9/00—Treating solid fuels to improve their combustion
    • C10L9/10—Treating solid fuels to improve their combustion by using additives
    • 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
    • C10L1/12—Inorganic compounds
    • C10L1/1266—Inorganic compounds nitrogen containing compounds, (e.g. NH3)
    • 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
    • C10L1/16—Hydrocarbons
    • C10L1/1616—Hydrocarbons fractions, e.g. lubricants, solvents, naphta, bitumen, tars, terpentine
    • 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
    • C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
    • C10L1/1822—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
    • C10L1/1824—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy

Definitions

  • This invention relates to novel compositions for use in fuels, gasoline, diesel, coal, and biodiesel, and processes for making the same.
  • an object of this invention is to provide an improved fuel additive for use with gasoline, diesel fuels, biodiesel, natural gas, coal fuels, and biomass fuels that provides at least one of the following benefits: an increase in power; an increase in combustion efficiency; an increase in fuel mileage; a smoother running engine; reduced fouling of the fuel system; cleaning the fuel system, including injectors; and diminishing "diesel rap" in diesel engines.
  • Another object of this invention is to improve home heating systems that use oil by providing at least one of the following benefits: better fuel atomization; hotter flame temperatures; more complete combustion; and less soot generation.
  • Yet another object of this invention is to improve coal-fired systems by providing at least one of the following benefits: better fuel atomization for coal-oil slurries; hotter flame temperatures; more complete combustion; and less soot generation.
  • the inventive subject matter comprises a fuel additive concentrate comprising: an alkali metal nitrate; and a organic solvent.
  • a fuel additive comprising: the concentrate above in a ratio of 1 part concentrate to about 10 to about 11 parts organic solvent.
  • the fuel additive above, wherein the organic solvent is selected from isopropanol, methanol, ethanol, gasoline, diesel, biodiesel, C1-C12 hydrocarbons, C1-C6 alcohols, and combinations thereof.
  • a process of treating fuel comprising: adding the fuel additive above to fuel in a ratio selected from about 1 unit to a range of about 3000 to about 20,000 units.
  • a fuel composition which comprises gasoline and a fuel additive comprising an alkali metal nitrate in a organic solvent.
  • a fuel composition which comprises diesel fuel and a fuel additive comprising an alkali metal nitrate in a organic solvent.
  • a fuel composition which comprises biodiesel and a fuel additive comprising an alkali metal nitrate in a organic solvent.
  • a fuel composition comprising coal and a fuel additive comprising an alkali metal nitrate in a organic solvent.
  • a fuel composition comprising jet fuel and a fuel additive comprising an alkali metal nitrate in a organic solvent.
  • a fuel composition comprising fuel oil and a fuel additive comprising an alkali metal nitrate in a organic solvent.
  • a fuel composition comprising a gasoline-ethanol mixture and a fuel additive comprising an alkali metal nitrate in a organic solvent.
  • a method for improving the operation of a gasoline-powered, artificial ignition, internal combustion engine comprising providing to said engine a fuel composition comprising gasoline and a fuel additive comprising an alkali metal nitrate in a organic solvent.
  • a method for improving the operation of a diesel-powered combustion engine comprising providing to said engine a fuel composition comprising diesel or biodiesel fuel and a fuel additive comprising an alkali metal nitrate in a organic solvent.
  • a method for improving the operation of a coal-powered boiler or power plant comprising providing to said engine a fuel composition comprising coal and a fuel additive comprising an alkali metal nitrate in a organic solvent.
  • a method for improving the operation of a jet engine comprising providing to said engine a fuel composition comprising jet fuel and a fuel additive comprising an alkali metal nitrate in a organic solvent.
  • a method for improving the operation of a boiler comprising providing to said boiler a fuel composition comprising fuel oil and a fuel additive comprising an alkali metal nitrate in a organic solvent.
  • the fuels which are contemplated for use in the fuel compositions of the present inventive subject matter are normally liquid hydrocarbon fuels in the gasoline boiling range, including hydrocarbon base fuels.
  • the term "petroleum distillate fuel” also is used to describe the fuels which can be utilized in the fuel compositions of the present inventive subject matter and which have the above characteristic boiling points. The term, however, is not intended to be restricted to straight-run distillate fractions.
  • the distillate fuel can be straight-run distillate fuel, catalytically or thermally cracked (including hydro cracked) distillate fuel, or a mixture of straight-run distillate fuel, naphthas and the like with cracked distillate stocks.
  • the base fuels used in the formation of the fuel compositions of the present inventive subject matter can be treated in accordance with well-known commercial methods, such as acid or caustic treatment, hydrogenation, solvent refining, clay treatment, etc.
  • Gasolines are supplied in a number of different grades depending on the type of service for which they are intended.
  • the gasolines utilized in the present inventive subject matter include those designed as motor and aviation gasolines.
  • Motor gasolines include those defined by ASTM specification D-439-73 and are composed of a mixture of various types of hydrocarbons including aromatics, olefins, paraffins, isoparaffins, napthenes and occasionally diolefins.
  • Motor gasolines normally have a boiling range within the limits of about 7O.degree. F. to 45O.degree. F. while aviation gasolines have narrower boiling ranges, usually within the limits of about lOO.degree. F. to 330. degree. F.
  • diesel fuel as defined by the American Society of Testing and Management (ASTM) Standard Specification for Fuel Oils (designation D 396-86) or any of grade numbers 1-D, 2-D or 4-D, as specified in ASTM D 975. More generally, diesel fuel can be a fuel oil No. 2 or No. 4 petroleum distillates as well as alternative diesel fuels containing emulsified water or alcohols such as ethanol or methanol, very low sulfur fuels (less than 0.05% sulfur), diesel fuel blends with bioderived components (animal and vegetable fats and oils, fractions and derivatives), and the like, as long as they exhibit volatility and cetane number characteristics effective for the purpose.
  • ASTM American Society of Testing and Management
  • Diesel fuels will typically have a 90% distillation point within the range of 300 degree to 390 degree C. and a viscosity of from 1 to 25 centistokes at 40. degree. C.
  • Biodiesel includes fuels made from vegetable oils, including those modified to be microemulsion diesel fuels by addition of low carbon chain alcohols such as methanol, ethanol, or butanol, as well as alkali soaps (stearates, oleates, etc.).
  • This inventive subject matter also contemplates the use of the fuel compositions in ethanol with gasoline, fuel alcohol, natural gas, coal, and biomass.
  • the present inventive subject matter concerns lithium salts, esters, and so forth prepared with solvents to form fuel combustion and efficiency improvers.
  • lithium has a molar mass of 6.941 g/mol.
  • Preferred salts of the present inventive subject matter comprise nitrates. Nitrates are well known in the field of explosives and are known oxidizers. Powdered lithium nitrate anhydrous is reported to be an oxidizing agent and flame colorant used in the manufacture of fireworks and flares.
  • the alkali metal nitrate salts herein can be expressed in terms of molar ratios.
  • lithium has an atomic mass of 6.939 g/mol.
  • Nitrate, comprising X-NO 3 comprises one nitrogen and three oxygen atoms.
  • Nitrogen has an atomic mass of 14.0067 g/mol
  • oxygen has an atomic mass of 15.994 g/mol
  • one mole of NO 3 weighs 62.0049 grams.
  • one mole of LiNO 3 has a calculated weight of about 68.9439 grams.
  • the inventive subject matter includes fuel additive super concentrate (SC), a fuel additive (FA), and treated fuel.
  • SC fuel additive super concentrate
  • FA fuel additive
  • treated fuel a fuel additive
  • an unusual feature is the dissolution of an inorganic salt into an organic solvent.
  • super concentrate and concentrate are used interchangeably.
  • These compositions are made using a quantitative range of LiNO 3 amounts. Preferred ranges of LiNO 3 comprise 0.5 mol - 2.5 mol, more preferably 0.8 mol - 2.0 mol, more preferably 0.9 mol - 1.5 mol, and more preferably 0.9 mol - 1.2 mol.
  • Preferred ranges also comprise 1.0 mol - 1.16 mol, 1.12 mol - 1.16 mol, and 1.12 mol - 1.18 mol, as contemplated within the subject matter of the inventive subject matter. More specifically, per liter of solvent, concentrate may be made by adding the alkali metal salt, e.g. LiNO 3 , in the molar amounts listed herein, e.g. 2.5, 2.0, 1.5, 1.2, 1.18, 1.16, 1.12, 1.0, 0.9, 0.8, 0.6, 0.58, 0.56, and 0.5 mol.
  • the alkali metal salt e.g. LiNO 3
  • solvents are used to create the super concentrate (SC) as well as being used as a diluent for the fuel additive (FA).
  • the solvent and diluent may be the same or different between the SC and the FA and a single solvent/diluent or a combinations of solvents/diluents are used in both the SC and the FA.
  • solvent and diluent refer to the step of the process in which they are being used, e.g. making the concentrate or making the additive, but the term solvent may also refer to the liquid portion of the solution being prepared.
  • Solvents which may be used in the present inventive subject matter include isopropanol (isopropyl alcohol), ethanol, Cl-ClO alkyl alcohols, gasoline, diesel fuel, biodiesel fuel, and solvent forms of primary, secondary, and mixed C1-C12 hydrocarbons. Isopropanol, methanol, ethanol, C1-C4 alkyl alcohols and mixtures thereof are preferred.
  • Specific solvent and diluent combinations contemplated for creating the concentrate include 50-50 IPA/Ethanol, IPA 0-100% plus Ethanol 100-0%, IPA in concentrate with alcohol diluent, IPA for concentrate with gasohol 85 as diluent, and alcohol for concentrate with IPA as diluent.
  • solvents are specifically recited herein, it is also within the knowledge of any ordinary chemist and intended to be included herein that other solvents or mixtures of solvents, besides those listed above, may be used with the metal nitrate salts herein to prepare the SC, the FA, and the fuel to be treated.
  • the solvents are used herein to make the concentrate as well as a diluent to convert the concentrate to the fuel additive product.
  • the solvent for the concentrate may be the same or different from the diluent.
  • the present inventive subject matter provides about 0.1 ppm Li in fuel.
  • the ppm of Li in fuel ranges from about 0.025 to about 1.0, and from about 0.05 to about 0.5, and from about 0.075 to about 0.25, and from about 0.09 to about 0.15, and any numerical ranges therebetween.
  • the amount of Li in fuel provides a range of combustion yield increases, including from about 5%-30% increase in yield, about 10%-25% increase in yield, about 18%-22% increase in yield, and about 10%- 15% increase in yield, with yield ranges including the numerical values therebetween as well.
  • Typical yield increases are about 4-10% depending on the quality of the fuel. Yield is measured by vehicle fuel economy, by increase in Btu's produced, and by other similar known methods.
  • EXAMPLE 1 - LiNO 3 super concentrate - isopropanol A process of preparing a lithium nitrate super concentrate comprises mixing into solution 1.69 moles of lithium nitrate in 15.23 moles isopropanol. This provides a LiNO 3 super concentrate.
  • a process of preparing a lithium nitrate concentrate comprises mixing into solution 1.69 moles of lithium nitrate in 19.54 moles ethanol. This provides a LiNO 3 super concentrate.
  • a process of preparing a lithium nitrate concentrate comprises mixing into solution 1.69 moles of lithium nitrate in 32.33 moles methanol. This provides a LiNO 3 super concentrate.
  • a process of preparing a lithium nitrate super concentrate comprises mixing into solution 0.85 moles of lithium nitrate in 15.23 moles isopropanol. This provides a LiNO 3 super concentrate.
  • a process of preparing a lithium nitrate concentrate comprises mixing into solution 0.85 moles of lithium nitrate in 19.54 moles ethanol. This provides a LiNO 3 super concentrate.
  • a process of preparing a lithium nitrate concentrate comprises mixing into solution 0.85 moles of lithium nitrate in 32.33 moles methanol. This provides a LiNO 3 super concentrate.
  • a process of preparing a fuel additive comprises diluting a super concentrate as described herein in a ratio of about 1 part to about 11 parts solvent/diluent.
  • a process of preparing a fuel additive comprises diluting a super concentrate as described herein in a ratio of about 1 part to about 10 parts solvent/diluent.
  • EXAMPLE 9 Li with isopropanol diluent
  • a process of preparing a lithium nitrate fuel additive (FA) which comprises diluting a lithium nitrate superconcentrate in a ratio of about 1 part concentrate to about 10 to 11 parts isopropanol (total of 11 or 12 parts, respectively).
  • a process of preparing a lithium nitrate fuel additive (FA) which comprises diluting a lithium nitrate super concentrate in a ratio of about 1 part concentrate to about 10 to
  • a process of preparing a super concentrate fuel additive which comprises combining one or more nitrate salts of an alkali metal and mixing into a chemically reasonable solvent, creating a 3%-20% concentrate solution.
  • a process of preparing a fuel additive which comprises diluting a 3%-20% super concentrate solution in a ratio of about 1 part concentrate to about 5 to about 20 parts solvent.
  • a process of treating fuel or enhancing combustion of a fuel source which comprises mixing about 1 liter of fuel additive (FA) to about 3000 to 4000 liters of fuel.
  • FA fuel additive
  • a process of treating fuel or enhancing combustion of a fuel source which comprises mixing about 1 liter of fuel additive to a range of about 2000 liters to about 15,000 liters of fuel.
  • a process of treating fuel or enhancing combustion of a fuel source which comprises mixing about 1 liter of fuel additive to a range of about 6000 liters to about 15,000 liters of fuel.
  • a process of treating fuel or enhancing combustion of a fuel source which comprises mixing about 1 liter of fuel additive to a range of about 10,000 liters to about 20,000 liters of fuel.
  • a process of preparing a fuel additive which comprises diluting a 3%-20% concentrate solution in a ratio of 1 part concentrate to from about 5 to about 20 parts biodiesel fuel plus diesel fuel combination.
  • a process of preparing a fuel additive which comprises diluting a 3%-20% concentrate solution in a ratio of 1 part concentrate to from about 5 to about 20 parts biodiesel fuel.
  • a process of preparing a fuel additive which comprises diluting a 3%-20% concentrate solution in a ratio of 1 part concentrate to from about 5 to about 20 parts diesel fuel.
  • a process of preparing a fuel additive which comprises diluting a 3%-20% concentrate solution in a ratio of 1 part concentrate to from about 5 to about 20 parts ethanol with gasoline fuel.
  • a process of treating fuel or enhancing combustion of a fuel source which comprises mixing about 1 liter of fuel additive to a range of about 4000 to about 10,000, or about
  • a process of preparing a fuel additive which comprises diluting a 3%-20% concentrate solution in a ratio of 1 part concentrate to 1 part fuel alcohol.
  • a process of treating boiler fuel e.g. DIESEL 2, DIESEL 6 OR BUNKER OIL, which comprises mixing about 1 unit fuel additive to about 4,000 units of fuel.
  • EXAMPLE 25 A process of treat coal or biomass fuel for combustion where the fuel additive is added directly into the burner at equivalent volumes.
  • a process of preparing a fuel additive which comprises diluting a superconcentrate as described herein with a diluent of IPA mixed with Ethanol in a 50/50 ratio.
  • a process of preparing a fuel additive which comprises diluting a superconcentrate as described herein with a diluent of IPA 0%-100% mixed with Ethanol 100%-0%.
  • a process of preparing a fuel additive which comprises diluting a superconcentrate made with IPA as described herein with a diluent of ethanol.
  • a process of preparing a fuel additive which comprises diluting a superconcentrate made with IPA as described herein with a diluent of gasohol.
  • a process of preparing a fuel additive which comprises diluting a superconcentrate made with ethanol as described herein with a diluent of IPA.
  • Fuel additive was added to diesel fuel used in a boat engine. It was observed that fuel consumption decreased 13.5% and power increased 12.5% according to the On-Board
  • HFRR High Frequency Reciprocating Rig
  • lubricity measured at 690 urn shows increased wear at the rotor pin groove, and the washer disc housing.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Health & Medical Sciences (AREA)
  • Emergency Medicine (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

La présente invention porte sur des compositions novatrices pour carburants, essence, diesel, charbon, éthanol, biodiesel et sur les processus de fabrication correspondants.
EP07759620A 2006-03-28 2007-03-28 Additifs de carburant Withdrawn EP2029703A2 (fr)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US78640306P 2006-03-28 2006-03-28
US80278006P 2006-05-24 2006-05-24
US82073606P 2006-07-28 2006-07-28
PCT/US2007/065407 WO2007112456A2 (fr) 2006-03-28 2007-03-28 Additifs de carburant

Publications (1)

Publication Number Publication Date
EP2029703A2 true EP2029703A2 (fr) 2009-03-04

Family

ID=38541905

Family Applications (1)

Application Number Title Priority Date Filing Date
EP07759620A Withdrawn EP2029703A2 (fr) 2006-03-28 2007-03-28 Additifs de carburant

Country Status (6)

Country Link
EP (1) EP2029703A2 (fr)
BR (1) BRPI0709261A2 (fr)
CA (1) CA2647538A1 (fr)
EA (1) EA200870381A1 (fr)
MX (1) MX2008012585A (fr)
WO (1) WO2007112456A2 (fr)

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
BRPI0900414A2 (pt) * 2009-02-06 2010-12-07 Carlos Ernesto Covalski processo para obtenção de combustìvel a partir da mescla de biodiesel com álcool etìlico anidro
CN102031163B (zh) * 2009-09-29 2013-07-10 济南开发区星火科学技术研究院 一种乙醇汽油复合添加剂及其制备方法
US10718511B2 (en) 2010-07-02 2020-07-21 Harry R. Taplin, JR. System for combustion of fuel to provide high efficiency, low pollution energy
US8852300B2 (en) 2010-07-02 2014-10-07 Harry R. Taplin, JR. Lithium conditioned engine with reduced carbon oxide emissions
CZ306196B6 (cs) * 2011-10-13 2016-09-21 Česká zemědělská univerzita v Praze Palivo na bázi bionafty
CN103911192B (zh) * 2014-04-01 2015-04-22 湖南华远新能源有限公司 用于改善生物柴油雾化性能的添加剂、制备方法及应用

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4002558A (en) * 1976-01-22 1977-01-11 Exxon Research And Engineering Company Removing water haze from distillate fuels

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2007112456A3 *

Also Published As

Publication number Publication date
WO2007112456A2 (fr) 2007-10-04
MX2008012585A (es) 2009-07-27
WO2007112456A3 (fr) 2008-06-12
EA200870381A1 (ru) 2009-04-28
BRPI0709261A2 (pt) 2011-06-28
CA2647538A1 (fr) 2007-10-04

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