[go: up one dir, main page]

US20050091913A1 - Method for reducing combustion chamber deposit flaking - Google Patents

Method for reducing combustion chamber deposit flaking Download PDF

Info

Publication number
US20050091913A1
US20050091913A1 US10/696,618 US69661803A US2005091913A1 US 20050091913 A1 US20050091913 A1 US 20050091913A1 US 69661803 A US69661803 A US 69661803A US 2005091913 A1 US2005091913 A1 US 2005091913A1
Authority
US
United States
Prior art keywords
manganese
manganese tricarbonyl
containing compound
tricarbonyl
fuel
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
Application number
US10/696,618
Inventor
Allen Aradi
James Smith
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.)
Afton Chemical Corp
Original Assignee
Afton Chemical Corp
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 Afton Chemical Corp filed Critical Afton Chemical Corp
Priority to US10/696,618 priority Critical patent/US20050091913A1/en
Assigned to ETHYL PETROLEUM ADDITIVES, INC. reassignment ETHYL PETROLEUM ADDITIVES, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: ARADI, ALLEN A., SMITH, JAMES B.
Assigned to SUNTRUST BANK, AS ADMINISTRATIVE AGENT reassignment SUNTRUST BANK, AS ADMINISTRATIVE AGENT SECURITY AGREEMENT Assignors: ETHYL PETROLEUM ADDITIVES, INC.
Priority to CA2677761A priority patent/CA2677761C/en
Priority to CA002482735A priority patent/CA2482735C/en
Priority to AU2004218620A priority patent/AU2004218620A1/en
Priority to MXPA04010020A priority patent/MXPA04010020A/en
Priority to DE602004030408T priority patent/DE602004030408D1/en
Priority to EP04024823A priority patent/EP1528097B1/en
Priority to AT04024823T priority patent/ATE491012T1/en
Priority to ZA2004/08543A priority patent/ZA200408543B/en
Priority to JP2004309792A priority patent/JP2005133720A/en
Priority to ARP040103895A priority patent/AR046559A1/en
Priority to RU2004131494/06A priority patent/RU2283437C2/en
Priority to SG200406302A priority patent/SG111280A1/en
Priority to CN2010102753375A priority patent/CN101914397A/en
Priority to CNA2004100921718A priority patent/CN1637120A/en
Priority to KR1020040086425A priority patent/KR20050040783A/en
Priority to BR0404762-1A priority patent/BRPI0404762A/en
Assigned to AFTON CHEMICAL CORPORATION reassignment AFTON CHEMICAL CORPORATION CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: ETHYL PETROLEUM ADDITIVES, INC.
Publication of US20050091913A1 publication Critical patent/US20050091913A1/en
Assigned to SUNTRUST BANK reassignment SUNTRUST BANK SECURITY AGREEMENT Assignors: AFTON CHEMICAL CORPORATION
Assigned to AFTON CHEMICAL CORPORATION reassignment AFTON CHEMICAL CORPORATION RELEASE BY SECURED PARTY (SEE DOCUMENT FOR DETAILS). Assignors: SUNTRUST BANK
Abandoned legal-status Critical Current

Links

Classifications

    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/182Organic compounds containing oxygen containing hydroxy groups; Salts thereof
    • C10L1/1828Salts thereof
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M27/00Apparatus for treating combustion-air, fuel, or fuel-air mixture, by catalysts, electric means, magnetism, rays, sound waves, or the like
    • F02M27/02Apparatus for treating combustion-air, fuel, or fuel-air mixture, by catalysts, electric means, magnetism, rays, sound waves, or the like by catalysts
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1216Inorganic compounds metal compounds, e.g. hydrides, carbides
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1225Inorganic compounds halogen containing compounds
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • 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
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1266Inorganic compounds nitrogen containing compounds, (e.g. NH3)
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1275Inorganic compounds sulfur, tellurium, selenium containing compounds
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1283Inorganic compounds phosphorus, arsenicum, antimonium containing compounds
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/1814Chelates
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/188Carboxylic acids; metal salts thereof
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2431Organic compounds containing sulfur, selenium and/or tellurium sulfur bond to oxygen, e.g. sulfones, sulfoxides
    • C10L1/2437Sulfonic acids; Derivatives thereof, e.g. sulfonamides, sulfosuccinic acid esters
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/26Organic compounds containing phosphorus
    • C10L1/2608Organic compounds containing phosphorus containing a phosphorus-carbon bond
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/30Organic compounds compounds not mentioned before (complexes)
    • C10L1/301Organic compounds compounds not mentioned before (complexes) derived from metals
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/30Organic compounds compounds not mentioned before (complexes)
    • C10L1/305Organic compounds compounds not mentioned before (complexes) organo-metallic compounds (containing a metal to carbon bond)
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • 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
    • 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 OR C10K; LIQUIFIED PETROLEUM GAS; USE OF ADDITIVES TO FUELS OR FIRES; FIRE-LIGHTERS
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/04Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M25/00Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture

Definitions

  • the present invention is directed to a method of reducing combustion chamber deposit flaking, and consequently, reducing cold start emissions.
  • the method includes combustion of a fuel having a fuel additive containing a metallic compound.
  • the metallic compound is a manganese-containing compound.
  • Spark ignited internal combustion engines (carbureted, port fuel injection “PFI”, multiple point injection “MPI”, direct-injection gasoline “DIG”, etc.) accumulate combustion chamber deposits (CCD) during operation.
  • This deposit is a result of both inefficient combustion of the fuel during the power stroke, and thermal polymerization reactions of certain fuel components to give high molecular weight material that does not burn very well.
  • the deposit layers both on cylinder head surfaces inside the combustion chamber and on piston tops.
  • the piston top deposit in particular is fuel and moisture sensitive, and tends to curl and slough off when the deposit is fuel wetted and/or exposed to moisture. The symptoms of this flaking manifest themselves during cold start cranking when the combustion charge blows the sloughed off deposit from the combustion chamber and into the exhaust valve seats.
  • the emission control changes being made have resulted in cold start difficulties ascribed to the higher fueling rates during cold start causing combustion chamber deposits to flake off and become lodged in the exhaust valve sealing band area, thereby preventing a good seal during compression and hence leading to misfires.
  • the OBD system detects this immediately because of the subsequent elevated hydrocarbon emissions due to unburned fuel, and illuminates the malfunction indicator light (MIL) on the dashboard, necessitating a visit to the dealership for corrective repairs.
  • Cold start difficulties due to CCD flaking tend to occur mainly in higher displacement engines with more cylinders (6, 8, and 10 cylinder engines) because in these bigger engines the cranking rate is lower, and it takes longer to blow the flaked deposits away from the exhaust valves.
  • Combustion chamber deposit (CCD) flaking has been discovered to be reduced and even eliminated with the use of a fuel additive containing a metallic compound.
  • a manganese-containing compound, MMT completely suppresses CCD flaking.
  • a method of reducing combustion chamber deposit flaking in spark ignited internal combustion engines that experience combustion chamber deposits comprises the steps of supplying a fuel comprising an additive that includes a metal-containing compound to a spark ignited internal combustion engine, wherein the metal-containing compound is supplied in an amount effective to reduce combustion chamber deposit flaking.
  • the metal-containing compound may be a compound containing one or more of the following metals: manganese, platinum, palladium, rhodium, iron, cerium, copper, nickel, silver, cobalt and molybdenum, and mixtures thereof.
  • manganese platinum, palladium, rhodium, iron, cerium, copper, nickel, silver, cobalt and molybdenum, and mixtures thereof.
  • An example of a manganese compound is described in detail herein, but other metal-containing additives may be used.
  • the metal compound in the fuel is combusted in a spark ignited internal combustion engine. Use of the metal—containing additive reduces or eliminates CCD flaking.
  • the fuels and additives herein are adapted to be combusted in any spark ignited internal combustion engine.
  • Specific engines that will benefit include those having carbureted systems, port fuel injection systems, multi point injection systems, and direct injection gasoline systems. Also, turbocharged and supercharged versions of the foregoing will benefit. Other engines having advanced emissions controls, including for example exhaust gas recirculation, will benefit. Additionally, Otto cycle and two-stroke internal combustion engines will benefit.
  • the nonleaded or unleaded gasoline bases in the present fuel composition are conventional motor fuel distillates boiling in the general range of about 70° F. to 440° F. They include substantially all grades of unleaded gasoline presently being employed in spark ignition internal combustion engines. Generally they contain both straight runs and cracked stock, with or without alkylated hydrocarbons, reformed hydrocarbons and the like.
  • Such gasolines can be prepared from saturated hydrocarbons, e.g., straight stocks, alkylation products and the like, with detergents, antioxidants, dispersants, metal deactivators, rust inhibitors, multi-functional additives, demulsifiers, fluidizer oils, anti-icing, combustion catalysts, corrosion inhibitors, emulsifiers, surfactants, solvents or other similar and known additives. It is contemplated that in certain circumstances these additives may be included in concentrations above normal levels.
  • the base gasoline will be a blend of stocks obtained from several refinery processes.
  • the final blend may also contain hydrocarbons made by other procedures such as alkylates made by the reaction of C.sub.4 olefins and butanes using an acid catalyst such as sulfuric acid or hydrofluoric acid, and aromatics made from a reformer.
  • the motor gasoline bases used in formulating the fuel blends of this invention generally have initial boiling points ranging from about 70° F. to about 100° F. and final boiling points ranging from about 420° F. to about 440° F. as measured by the standard ASTM distillation procedure (ASTM D-86). Intermediate gasoline fractions boil away at temperatures within these extremes.
  • base gasolines having a low sulfur content as the oxides of sulfur tend to contribute to the irritating and choking characteristics of smog and other forms of atmospheric pollution.
  • the base gasolines should contain not more than about 100 ppm of sulfur in the form of conventional sulfur-containing impurities.
  • Another alternative includes fuels in which the sulfur content is no more than about 30 ppm.
  • the gasoline bases which this invention employs should be lead-free or substantially lead-free.
  • the gasoline may contain antiknock quantities of other agents such as cyclopentadienyl nickel nitrosyl, N-methyl aniline, and the like. Antiknock promoters such as 2.4 pentanedione may also be included.
  • supplemental valve and valve seat recession protectants include; boron oxides, bismuth oxides, ceramic bonded CaF.sub.2, iron phosphate, tricresylphosphate, phosphorus and sodium based additives and the like.
  • the fuel may further contain antioxidants such as 2,6 di-tert-butylephenol, 2,6-di-tert-buyl-p-cresol, phenylenediamines such as N—N.sup.1-di-sec-butyl-p-pheylenediamine, N-isopropylphenylenediamine, and the like.
  • the gasoline may contain dyes, metal deactivators, or other additives recognized to serve some useful purpose. The descriptive characteristics of one common base gasoline is given as follows. Obviously many other standard and specialized gasoline can be used in Applicants' fuel blend.
  • One metal that may be used includes elemental and ionic manganese, precursors thereof, and mixtures of metal compounds including manganese. These manganese compounds may be either inorganic or organic. Also effective is the generation, liberation or production in situ of manganese or manganese ions.
  • Inorganic metallic compounds in an example can include by example and without limitation fluorides, chlorides, bromides, iodides, oxides, nitrates, sulfates, phosphates, nitrides, hydrides, hydroxides, carbonates and mixtures thereof.
  • Metal sulfates and phosphates will be operative and may, in certain fuels and combustion applications, not present unacceptable additional sulfur and phosphorus combustion byproducts.
  • Organometallic compounds in an example include alcohols, aldehydes, ketones, esters, anhydrides, sulfonates, phosphonates, chelates, phenates, crown ethers, carboxylic acids, amides, acetyl acetonates, and mixtures thereof.
  • Exemplary manganese containing organometallic compounds are manganese tricarbonyl compounds. Such compounds are taught, for example, in U.S. Pat. Nos. 4,568,357; 4,674,447; 5,113,803; 5,599,357; 5,944,858 and European Patent No. 466 512 B1.
  • Suitable manganese tricarbonyl compounds which can be used include cyclopentadienyl manganese tricarbonyl, methylcyclopentadienyl manganese tricarbonyl, dimethylcyclopentadienyl manganese tricarbonyl, trimethylcyclopentadienyl manganese tricarbonyl, tetramethylcyclopentadienyl manganese tricarbonyl, pentamethylcyclopentadienyl manganese tricarbonyl, ethylcyclopentadienyl manganese tricarbonyl, diethylcyclopentadienyl manganese tricarbonyl, propylcyclopentadienyl manganese tricarbonyl, isopropylcyclopentadienyl manganese tricarbonyl, tert-butylcyclopentadienyl manganese tricarbonyl, octylcyclopentadienyl manganese tricarbonyl, do
  • cyclopentadienyl manganese tricarbonyls which are liquid at room temperature such as methylcyclopentadienyl manganese tricarbonyl, ethylcyclopentadienyl manganese tricarbonyl, liquid mixtures of cyclopentadienyl manganese tricarbonyl and methylcyclopentadienyl manganese tricarbonyl, mixtures of methylcyclopentadienyl manganese tricarbonyl and ethylcyclopentadienyl manganese tricarbonyl, etc.
  • the metal-containing compound When formulating additives to be used in the methods herein, the metal-containing compound must be employed in amounts sufficient to reduce or eliminate CCD flaking in the spark ignited internal combustion engine.
  • the amounts will vary according to the particular metal or mixture of metals and metal-containing compounds.
  • the amount of manganese added can be about 1 to about 50 mg manganese per liter.
  • the metal-containing compounds are believed to act as both a free radical sink and a combustion catalyst.
  • a radical sink the compounds may be inhibiting radical initiated fuel polymerization reactions hence limiting contribution to hydrocarbonaceous CCD by this route.
  • the manganese for instance, catalytically participates in the CCD removal mechanism by promoting carbon oxidation at lower temperatures.
  • cold start emissions refers to and is defined herein in accordance with the industry definition.
  • the industry recognized definition of cold-start emissions can be found in the FTP-75 (Federal Test Procedure). Details of the test procedure are described in the Code of Federal Regulations (CFR 40, Part 86). Briefly, the test procedure consists of the following three phases: 1) Cold-start, 2) Transient, and 3) Hot-start.
  • the FTP-75 emissions cycle simulates 11.04 miles (17.77 km) distance of travel in a time of 1874 seconds at an average speed of 21.2 mph (34.1 km/h). Before the test, the vehicle is conditioned overnight at 25+/ ⁇ 5 C to assure cold start conditions. The cold start is initiated followed by the transient phase.
  • the vehicle is shut down for a hot soak of 10 minutes before being restarted to perform the hot phase.
  • the emissions from each phase are collected in a separate Teflon bag for each test phase, and analyzed. Quantities of each emission component (HC, CO, CO 2 , NOx, etc) are expressed in g/mile (g/km) for each phase.
  • HC hydrocarbon emissions
  • the cold-start phase is the most important because it contributes 80-90% of the total from the three phases.
  • Fuels that included and did not include a metal-containing compound were compared in an engine test.
  • Manganese in MMT® was the additive used at a treat rate 8.25 mg. of manganese per liter of fuel.
  • the vehicle used in this study was a Dodge Intrepid with a six cylinder engine. It was operated for 3000 miles on the test cycle while fueled with non additized CITGO RUL gasoline. At the end of the test the engine was dismantled and rated for CCD flaking according to a procedure adapted from that published by Gautam T. Kalghatgi in the SAE Paper Series 2002-01-2833.
  • the use of the specific metal-containing additive noted completely eliminated flaking of combustion chamber deposits. In other words, no CCD flaked off when the additive was used.
  • Other metal-containing additives may be used, and the treat rate of any additive may be varied. By changing the selection of additive and/or the treat rate of the additive, the amount of reduction in flaking may be controlled. It is believed that, in the case of a manganese-containing additive, a treat rate of about two mg. of manganese per liter of fuel will achieve up to about a 50% reduction in CCD flaking.
  • the reactants and components are identified as ingredients to be brought together either in performing a desired chemical reaction (such as formation of the organometallic compound) or in forming a desired composition (such as an additive concentrate or additized fuel blend).
  • a desired chemical reaction such as formation of the organometallic compound
  • a desired composition such as an additive concentrate or additized fuel blend
  • the additive components can be added or blended into or with the base fuels individually per se and/or as components used in forming preformed additive combinations and/or sub-combinations.
  • the claims hereinafter may refer to substances, components and/or ingredients in the present tense (“comprises”, “is”, etc.), the reference is to the substance, components or ingredient as it existed at the time just before it was first blended or mixed with one or more other substances, components and/or ingredients in accordance with the present disclosure.
  • the fact that the substance, components or ingredient may have lost its original identity through a chemical reaction or transformation during the course of such blending or mixing operations or immediately thereafter is thus wholly immaterial for an accurate

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Inorganic Chemistry (AREA)
  • Emergency Medicine (AREA)
  • Health & Medical Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Combustion Methods Of Internal-Combustion Engines (AREA)
  • Catalysts (AREA)
  • Spark Plugs (AREA)
  • Ignition Installations For Internal Combustion Engines (AREA)

Abstract

A method reduces combustion chamber deposit flaking and spark ignited internal combustion engines. The method includes supplying a fuel having an additive that includes a metal-containing compound to a spark ignited internal combustion engine. The metal-containing compound is supplied in an amount effective to reduce combustion chamber deposit flaking. In one example, the metal is manganese and the additive compound is MMT. The reduction or elimination of combustion chamber deposit flaking means a reduction in cold start emissions from the engine.

Description

  • The present invention is directed to a method of reducing combustion chamber deposit flaking, and consequently, reducing cold start emissions. The method includes combustion of a fuel having a fuel additive containing a metallic compound. In one example, the metallic compound is a manganese-containing compound.
  • BACKGROUND
  • Spark ignited internal combustion engines (carbureted, port fuel injection “PFI”, multiple point injection “MPI”, direct-injection gasoline “DIG”, etc.) accumulate combustion chamber deposits (CCD) during operation. This deposit is a result of both inefficient combustion of the fuel during the power stroke, and thermal polymerization reactions of certain fuel components to give high molecular weight material that does not burn very well. The deposit layers both on cylinder head surfaces inside the combustion chamber and on piston tops. The piston top deposit in particular is fuel and moisture sensitive, and tends to curl and slough off when the deposit is fuel wetted and/or exposed to moisture. The symptoms of this flaking manifest themselves during cold start cranking when the combustion charge blows the sloughed off deposit from the combustion chamber and into the exhaust valve seats. The deposit flakes thus lodged in this new location wedge in the sealing band of the exhaust valves and prevent the tight sealing necessary to contain the fuel/air combustion charge during the compression stroke, thus inhibiting ignition and necessitating extended engine cranking periods to dislodge the deposit so that the engine can fire up normally. During this cranking, instead of the combustion charge being contained in the cylinder for the subsequent spark ignition, the combustion charge is prematurely expelled into the exhaust system and loads the catalytic converter with raw fuel. Some of this raw fuel escapes out of the exhaust aftertreatment system and may contribute to cold start hydrocarbon “HC” emissions. Also, when the engine does finally fire up, the subsequent hot combustion gases ignite this raw fuel. The ensuing vigorous combustion of raw fuel in the exhaust system may melt the catalytic converter due to the excessively high temperatures generated by this burn, and seriously damage the exhaust aftertreatment system.
  • The symptoms of CCD flaking have only recently been observed with the advent of advanced emissions control strategies aimed at lowering hydrocarbon emissions at cold start. The reasons for all these changes resulted from the discovery that a significant portion of total vehicular hydrocarbon emissions were generated during the initial 90 seconds it takes conventional, under the floor three-way catalytic converters to light off during cold start. Therefore, shortening this time interval became of paramount importance. Government environmental regulators also recognized this fact and mandated that vehicle manufacturers develop an on board diagnostic system (OBD) to monitor the emissions control system in a manner that would minimize hydrocarbon emissions to the environment, and this system be under warranty to ensure that it performed its intended task for the duration of the specified warranty period.
  • The emission control changes being made have resulted in cold start difficulties ascribed to the higher fueling rates during cold start causing combustion chamber deposits to flake off and become lodged in the exhaust valve sealing band area, thereby preventing a good seal during compression and hence leading to misfires. The OBD system detects this immediately because of the subsequent elevated hydrocarbon emissions due to unburned fuel, and illuminates the malfunction indicator light (MIL) on the dashboard, necessitating a visit to the dealership for corrective repairs. Cold start difficulties due to CCD flaking tend to occur mainly in higher displacement engines with more cylinders (6, 8, and 10 cylinder engines) because in these bigger engines the cranking rate is lower, and it takes longer to blow the flaked deposits away from the exhaust valves.
  • One way to deal with the cold start problem caused by CCD flaking is to not drive the vehicle a short distance under light load, thereby leaving the chamber to soak for extended periods of time. Another way to get around this problem is to simply continue cranking to blow away the offending deposit flakes, and on start up, rev up the engine for an additional thirty seconds to clean out the rest of the flaking deposit. However, this method inadvertantly leads to very high levels of hydrocarbon emissions and may cause the OBD MIL to illuminate.
  • DESCRIPTION
  • Combustion chamber deposit (CCD) flaking has been discovered to be reduced and even eliminated with the use of a fuel additive containing a metallic compound. In one example, a manganese-containing compound, MMT, completely suppresses CCD flaking.
  • A method of reducing combustion chamber deposit flaking in spark ignited internal combustion engines that experience combustion chamber deposits comprises the steps of supplying a fuel comprising an additive that includes a metal-containing compound to a spark ignited internal combustion engine, wherein the metal-containing compound is supplied in an amount effective to reduce combustion chamber deposit flaking.
  • The metal-containing compound may be a compound containing one or more of the following metals: manganese, platinum, palladium, rhodium, iron, cerium, copper, nickel, silver, cobalt and molybdenum, and mixtures thereof. An example of a manganese compound is described in detail herein, but other metal-containing additives may be used. In each alternative, the metal compound in the fuel is combusted in a spark ignited internal combustion engine. Use of the metal—containing additive reduces or eliminates CCD flaking.
  • The fuels and additives herein are adapted to be combusted in any spark ignited internal combustion engine. Specific engines that will benefit include those having carbureted systems, port fuel injection systems, multi point injection systems, and direct injection gasoline systems. Also, turbocharged and supercharged versions of the foregoing will benefit. Other engines having advanced emissions controls, including for example exhaust gas recirculation, will benefit. Additionally, Otto cycle and two-stroke internal combustion engines will benefit.
  • The nonleaded or unleaded gasoline bases in the present fuel composition are conventional motor fuel distillates boiling in the general range of about 70° F. to 440° F. They include substantially all grades of unleaded gasoline presently being employed in spark ignition internal combustion engines. Generally they contain both straight runs and cracked stock, with or without alkylated hydrocarbons, reformed hydrocarbons and the like. Such gasolines can be prepared from saturated hydrocarbons, e.g., straight stocks, alkylation products and the like, with detergents, antioxidants, dispersants, metal deactivators, rust inhibitors, multi-functional additives, demulsifiers, fluidizer oils, anti-icing, combustion catalysts, corrosion inhibitors, emulsifiers, surfactants, solvents or other similar and known additives. It is contemplated that in certain circumstances these additives may be included in concentrations above normal levels.
  • Generally, the base gasoline will be a blend of stocks obtained from several refinery processes. The final blend may also contain hydrocarbons made by other procedures such as alkylates made by the reaction of C.sub.4 olefins and butanes using an acid catalyst such as sulfuric acid or hydrofluoric acid, and aromatics made from a reformer.
  • The motor gasoline bases used in formulating the fuel blends of this invention generally have initial boiling points ranging from about 70° F. to about 100° F. and final boiling points ranging from about 420° F. to about 440° F. as measured by the standard ASTM distillation procedure (ASTM D-86). Intermediate gasoline fractions boil away at temperatures within these extremes.
  • It is also desirable to utilize base gasolines having a low sulfur content as the oxides of sulfur tend to contribute to the irritating and choking characteristics of smog and other forms of atmospheric pollution. To the extent it is economically feasible, the base gasolines should contain not more than about 100 ppm of sulfur in the form of conventional sulfur-containing impurities. Another alternative includes fuels in which the sulfur content is no more than about 30 ppm.
  • The gasoline bases which this invention employs should be lead-free or substantially lead-free. However, the gasoline may contain antiknock quantities of other agents such as cyclopentadienyl nickel nitrosyl, N-methyl aniline, and the like. Antiknock promoters such as 2.4 pentanedione may also be included. On certain occasions it will be desirable for the gasoline to contain supplemental valve and valve seat recession protectants. Nonlimiting examples include; boron oxides, bismuth oxides, ceramic bonded CaF.sub.2, iron phosphate, tricresylphosphate, phosphorus and sodium based additives and the like. The fuel may further contain antioxidants such as 2,6 di-tert-butylephenol, 2,6-di-tert-buyl-p-cresol, phenylenediamines such as N—N.sup.1-di-sec-butyl-p-pheylenediamine, N-isopropylphenylenediamine, and the like. Likewise, the gasoline may contain dyes, metal deactivators, or other additives recognized to serve some useful purpose. The descriptive characteristics of one common base gasoline is given as follows. Obviously many other standard and specialized gasoline can be used in Applicants' fuel blend.
    CHARACTERISTICS OF GASOLINES
    API Gravity (@ 60 F.) 50-70
    Reid Vapor Pressure, EPA, (psi) 6-8
    Sulfur (ppm)  0-500
    Research Octane  85-120
    Motor Octane 75-90
    R + M/2  87-110
    Oxygenates (%)  0-30
    Aromatics (%)  0-50
    Olefins (%)  0-30
    Paraffins (%)  30-100
    ASTM Distillation
    Vol % Evaporate Temp., F.
    IBP  70-100
     5 100-130
    10 120-140
    15 140-160
    20 150-170
    30 170-190
    40 190-210
    50 200-220
    60 220-240
    70 240-260
    80 280-300
    90 340-370
    95 380-400
    EP 420-440
  • One metal that may be used includes elemental and ionic manganese, precursors thereof, and mixtures of metal compounds including manganese. These manganese compounds may be either inorganic or organic. Also effective is the generation, liberation or production in situ of manganese or manganese ions.
  • Inorganic metallic compounds in an example can include by example and without limitation fluorides, chlorides, bromides, iodides, oxides, nitrates, sulfates, phosphates, nitrides, hydrides, hydroxides, carbonates and mixtures thereof. Metal sulfates and phosphates will be operative and may, in certain fuels and combustion applications, not present unacceptable additional sulfur and phosphorus combustion byproducts. Organometallic compounds in an example include alcohols, aldehydes, ketones, esters, anhydrides, sulfonates, phosphonates, chelates, phenates, crown ethers, carboxylic acids, amides, acetyl acetonates, and mixtures thereof.
  • Exemplary manganese containing organometallic compounds are manganese tricarbonyl compounds. Such compounds are taught, for example, in U.S. Pat. Nos. 4,568,357; 4,674,447; 5,113,803; 5,599,357; 5,944,858 and European Patent No. 466 512 B1.
  • Suitable manganese tricarbonyl compounds which can be used include cyclopentadienyl manganese tricarbonyl, methylcyclopentadienyl manganese tricarbonyl, dimethylcyclopentadienyl manganese tricarbonyl, trimethylcyclopentadienyl manganese tricarbonyl, tetramethylcyclopentadienyl manganese tricarbonyl, pentamethylcyclopentadienyl manganese tricarbonyl, ethylcyclopentadienyl manganese tricarbonyl, diethylcyclopentadienyl manganese tricarbonyl, propylcyclopentadienyl manganese tricarbonyl, isopropylcyclopentadienyl manganese tricarbonyl, tert-butylcyclopentadienyl manganese tricarbonyl, octylcyclopentadienyl manganese tricarbonyl, dodecylcyclopentadienyl manganese tricarbonyl, ethylmethylcyclopentadienyl manganese tricarbonyl, indenyl manganese tricarbonyl, and the like, including mixtures of two or more such compounds. In one alternative are the cyclopentadienyl manganese tricarbonyls which are liquid at room temperature such as methylcyclopentadienyl manganese tricarbonyl, ethylcyclopentadienyl manganese tricarbonyl, liquid mixtures of cyclopentadienyl manganese tricarbonyl and methylcyclopentadienyl manganese tricarbonyl, mixtures of methylcyclopentadienyl manganese tricarbonyl and ethylcyclopentadienyl manganese tricarbonyl, etc.
  • Preparation of such compounds is described in the literature, for example, U.S. Pat. No. 2,818,417, the disclosure of which is incorporated herein in its entirety.
  • When formulating additives to be used in the methods herein, the metal-containing compound must be employed in amounts sufficient to reduce or eliminate CCD flaking in the spark ignited internal combustion engine. The amounts will vary according to the particular metal or mixture of metals and metal-containing compounds. In the example of a manganese-containing compound, the amount of manganese added can be about 1 to about 50 mg manganese per liter.
  • The metal-containing compounds are believed to act as both a free radical sink and a combustion catalyst. As a radical sink, the compounds may be inhibiting radical initiated fuel polymerization reactions hence limiting contribution to hydrocarbonaceous CCD by this route. As a combustion catalyst, the manganese, for instance, catalytically participates in the CCD removal mechanism by promoting carbon oxidation at lower temperatures.
  • The term “cold start emissions” refers to and is defined herein in accordance with the industry definition. The industry recognized definition of cold-start emissions can be found in the FTP-75 (Federal Test Procedure). Details of the test procedure are described in the Code of Federal Regulations (CFR 40, Part 86). Briefly, the test procedure consists of the following three phases: 1) Cold-start, 2) Transient, and 3) Hot-start. The FTP-75 emissions cycle simulates 11.04 miles (17.77 km) distance of travel in a time of 1874 seconds at an average speed of 21.2 mph (34.1 km/h). Before the test, the vehicle is conditioned overnight at 25+/−5 C to assure cold start conditions. The cold start is initiated followed by the transient phase. Then the vehicle is shut down for a hot soak of 10 minutes before being restarted to perform the hot phase. The emissions from each phase are collected in a separate Teflon bag for each test phase, and analyzed. Quantities of each emission component (HC, CO, CO2, NOx, etc) are expressed in g/mile (g/km) for each phase. For hydrocarbon emissions (HC) the cold-start phase is the most important because it contributes 80-90% of the total from the three phases.
  • EXAMPLES
  • Fuels that included and did not include a metal-containing compound were compared in an engine test. Manganese in MMT® was the additive used at a treat rate 8.25 mg. of manganese per liter of fuel.
  • The vehicle used in this study was a Dodge Intrepid with a six cylinder engine. It was operated for 3000 miles on the test cycle while fueled with non additized CITGO RUL gasoline. At the end of the test the engine was dismantled and rated for CCD flaking according to a procedure adapted from that published by Gautam T. Kalghatgi in the SAE Paper Series 2002-01-2833.
  • Test Procedure: CCD Flaking Test on the Dodge Intrepid
  • Ethyl Test Outline:
    • Vehicle: Chrysler Dodge Intrepid
    • Fuel: CITGO Regular Unleaded
    • Test # 1: Without MMT Additive
    • Test # 2: With MMT Additive
    • Cycle: IVD Chassis Dyno Cycle (Average 45 mph)
      • Two shifts per day (about 600 miles)
      • Soak overnight
      • End test at a cumulative 3000 miles:
        At End of Test:
      • 1. Dismantle engine as per regular IVD/CCD test
      • 2. Measure deposit thickness on both the head and pistons using the template
      • 3. Spray piston tops with soap water (1 drop of liquid household detergent per 100 mL water) using a house plant water sprayer
      • 4. After 3 hours photograph piston tops and note extent of flaking
      • 5. Spray piston tops again and leave overnight.
      • 6. Photograph piston tops and note extend of flaking
      • 7. Remove flaked deposit by vacuum and weigh
      • 8. Photograph piston tops
      • 9. Measure thickness of remaining deposit using the template
      • 10. Scrape and total piston top deposit
      • 11. Complete IVD and CCD determination on head.
  • By the term “average” it is meant the average of deposit amounts on the six valves or the six piston tops, or the six cylinder head locations corresponding to the six pistons.
    TABLE 1
    The Manganese Containing Additive Inhibited CCD Flaking
    Flaked Amount of Total Engine CCD Engine IVD
    Additive CCD (milligrams) (milligrams) (milligrams)
    No 89.4 783.4 312.2
    Yes 0 688.9 305.9
  • As is evident from this test example, the use of the specific metal-containing additive noted completely eliminated flaking of combustion chamber deposits. In other words, no CCD flaked off when the additive was used. Other metal-containing additives may be used, and the treat rate of any additive may be varied. By changing the selection of additive and/or the treat rate of the additive, the amount of reduction in flaking may be controlled. It is believed that, in the case of a manganese-containing additive, a treat rate of about two mg. of manganese per liter of fuel will achieve up to about a 50% reduction in CCD flaking.
  • Given the discovered absence of CCD flaking, it should be evident that a more complete combustion occurs, especially during the cold start period of engine operation. There were no flakes to block the sealing of the exhaust valves. Therefore, less raw fuel is allowed to pass through the cylinder and into the exhaust system. Accordingly, cold start emissions of hydrocarbons should be reduced by use of the additive in spark ignited internal combustion engines that experience combustion chamber deposits.
  • It is to be understood that the reactants and components referred to by chemical name anywhere in the specification or claims hereof, whether referred to in the singular or plural, are identified as they exist prior to coming into contact with another substance referred to by chemical name or chemical type (e.g., base fuel, solvent, etc.). It matters not what chemical changes, transformations and/or reactions, if any, take place in the resulting mixture or solution or reaction medium as such changes, transformations and/or reactions are the natural result of bringing the specified reactants and/or components together under the conditions called for pursuant to this disclosure. Thus the reactants and components are identified as ingredients to be brought together either in performing a desired chemical reaction (such as formation of the organometallic compound) or in forming a desired composition (such as an additive concentrate or additized fuel blend). It will also be recognized that the additive components can be added or blended into or with the base fuels individually per se and/or as components used in forming preformed additive combinations and/or sub-combinations. Accordingly, even though the claims hereinafter may refer to substances, components and/or ingredients in the present tense (“comprises”, “is”, etc.), the reference is to the substance, components or ingredient as it existed at the time just before it was first blended or mixed with one or more other substances, components and/or ingredients in accordance with the present disclosure. The fact that the substance, components or ingredient may have lost its original identity through a chemical reaction or transformation during the course of such blending or mixing operations or immediately thereafter is thus wholly immaterial for an accurate understanding and appreciation of this disclosure and the claims thereof.
  • At numerous places throughout this specification, reference has been made to a number of U.S. Patents, published foreign patent applications and published technical papers. All such cited documents are expressly incorporated in full into this disclosure as if fully set forth herein.
  • This invention is susceptible to considerable variation in its practice. Therefore the foregoing description is not intended to limit, and should not be construed as limiting, the invention to the particular exemplifications presented hereinabove. Rather, what is intended to be covered is as set forth in the ensuing claims and the equivalents thereof permitted as a matter of law.
  • Patentee does not intend to dedicate any disclosed embodiments to the public, and to the extent any disclosed modifications or alterations may not literally fall within the scope of the claims, they are considered to be part of the invention under the doctrine of equivalents.

Claims (28)

1. A method of reducing combustion chamber deposit flaking in spark ignited internal combustion engines that experience combustion chamber deposits comprising the steps of:
supplying a fuel comprising an additive that includes a metal-containing compound to a spark ignited internal combustion engine,
wherein the metal-containing compound is supplied in an amount effective to reduce combustion chamber deposit flaking.
2. A method as described in claim 1, wherein the metal-containing compound comprises a metal selected from the group consisting of manganese, platinum, palladium, rhodium, iron, cerium, copper, nickel, silver, cobalt, and molybdenum, and mixtures thereof.
3. A method as described in claim 2, wherein the metal-containing compound comprises a manganese-containing compound.
4. The method described in claim 3, wherein the manganese-containing compound is an inorganic manganese compound.
5. The method described in claim 4, wherein the inorganic manganese compound is selected from the group consisting of fluorides, chlorides, bromides, iodides, oxides, nitrates, sulfates, phosphates, nitrides, hydrides, hydroxides, carbonates and mixtures thereof.
6. The method described in claim 3, wherein the manganese-containing compound is an organometallic compound.
7. The method described in claim 6, wherein the organometallic compound is selected from the group consisting of alcohols, aldehydes, ketones, esters, anhydrides, sulfonates, phosphonates, chelates, phenates, crown ethers, carboxylic acids, amides, acetyl acetonates and mixtures thereof.
8. The method described in claim 3, wherein the manganese-containing compound comprises about 1 to about 50 mgMn/liter of the fuel.
9. The method described in claim 6, wherein the organometallic compound comprises methylcyclopentadienyl manganese tricarbonyl.
10. The method described in claim 3, wherein the manganese-containing compound is selected from the following group: cyclopentadienyl manganese tricarbonyl, methylcyclopentadienyl manganese tricarbonyl, dimethylcyclopentadienyl manganese tricarbonyl, trimethylcyclopentadienyl manganese tricarbonyl, tetramethylcyclopentadienyl manganese tricarbonyl, pentamethylcyclopentadienyl manganese tricarbonyl, ethylcyclopentadienyl manganese tricarbonyl, diethylcyclopentadienyl manganese tricarbonyl, propylcyclopentadienyl manganese tricarbonyl, isopropylcyclopentadienyl manganese tricarbonyl, tert-butylcyclopentadienyl manganese tricarbonyl, octylcyclopentadienyl manganese tricarbonyl, dodecylcyclopentadienyl manganese tricarbonyl, ethylmethylcyclopentadienyl manganese tricarbonyl, indenyl manganese tricarbonyl, and the like, including mixtures of two or more such compounds.
11. A method as described in claim 1, wherein the fuel contains less than about 30 ppm of sulfur.
12. The method as described in claim 1, wherein the spark ignited internal combustion engine comprises a fuel injection system selected from the group consisting of the following: port fuel injection system, multi point injection system, and direct injection gasoline system.
13. The method as described in claim 1, wherein the fuel comprises regular, unleaded gasoline.
14. The method as described in claim 1, wherein the engine comprises six or more cylinders.
15. A method of reducing cold start emissions from spark-ignited internal combustion engines that experience combustion chamber deposits comprising the steps of:
supplying a fuel comprising an additive that includes a metal-containing compound to a spark ignited internal combustion engine;
wherein the metal-containing compound is supplied in an amount effective to reduce cold start emissions.
16. A method as described in claim 15, wherein the metal-containing compound comprises a metal selected from the group consisting of manganese, platinum, palladium, rhodium, iron, cerium, copper, nickel, silver, cobalt, and molybdenum, and mixtures thereof.
17. A method as described in claim 16, wherein the metal-containing compound comprises a manganese compound.
18. The method described in claim 17, wherein the manganese-containing compound is an inorganic manganese compound.
19. The method described in claim 18, wherein the inorganic manganese compound is selected from the group consisting of fluorides, chlorides, bromides, iodides, oxides, nitrates, sulfates, phosphates, nitrides, hydrides, hydroxides carbonates and mixtures thereof.
20. The method described in claim 17, wherein the manganese-containing compound is an organometallic compound.
21. The method described in claim 20, wherein the organometallic compound is selected from the group consisting of alcohols, aldehydes, ketones, esters, anhydrides, sulfonates, phosphonates, chelates, phenates, crown ethers, carboxylic acids, amides, acetyl acetonates and mixtures thereof.
22. The method described in claim 17, wherein the manganese-containing compound comprises about 1 to about 50 mgMn/liter of the fuel.
23. The method described in claim 20, wherein the organometallic compound comprises methylcyclopentadienyl manganese tricarbonyl.
24. The method described in claim 17, wherein the manganese-containing compound is selected from the following group: cyclopentadienyl manganese tricarbonyl, methylcyclopentadienyl manganese tricarbonyl, dimethylcyclopentadienyl manganese tricarbonyl, trimethylcyclopentadienyl manganese tricarbonyl, tetramethylcyclopentadienyl manganese tricarbonyl, pentamethylcyclopentadienyl manganese tricarbonyl, ethylcyclopentadienyl manganese tricarbonyl, diethylcyclopentadienyl manganese tricarbonyl, propylcyclopentadienyl manganese tricarbonyl, isopropylcyclopentadienyl manganese tricarbonyl, tert-butylcyclopentadienyl manganese tricarbonyl, octylcyclopentadienyl manganese tricarbonyl, dodecylcyclopentadienyl manganese tricarbonyl, ethylmethylcyclopentadienyl manganese tricarbonyl, indenyl manganese tricarbonyl, and the like, including mixtures of two or more such compounds.
25. A method as described in claim 15, where the fuel contains less than about 30 ppm of sulfur.
26. The method as described in claim 15, wherein the spark ignited internal combustion engine comprises a fuel injection system selected from the group consisting of the following: carbureted systems, port fuel injection system, multi point injection system, and direct injection gasoline system.
27. The method as described in claim 15, wherein the fuel comprises regular, unleaded gasoline.
28. The method as described in claim 15, wherein the engine comprises six or more cylinders.
US10/696,618 2003-10-29 2003-10-29 Method for reducing combustion chamber deposit flaking Abandoned US20050091913A1 (en)

Priority Applications (17)

Application Number Priority Date Filing Date Title
US10/696,618 US20050091913A1 (en) 2003-10-29 2003-10-29 Method for reducing combustion chamber deposit flaking
CA2677761A CA2677761C (en) 2003-10-29 2004-09-28 Method for reducing cold start emissions
CA002482735A CA2482735C (en) 2003-10-29 2004-09-28 Method for reducing combustion chamber deposit flaking
AU2004218620A AU2004218620A1 (en) 2003-10-29 2004-10-05 Method for reducing combustion chamber deposit flaking
MXPA04010020A MXPA04010020A (en) 2003-10-29 2004-10-12 Method for reducing combustion chamber deposit flaking.
DE602004030408T DE602004030408D1 (en) 2003-10-29 2004-10-19 Method for reducing the flaking of deposits in combustion chambers
AT04024823T ATE491012T1 (en) 2003-10-29 2004-10-19 METHOD FOR REDUCING DEPOSIT SHALLING IN COMBUSTION CHAMBERS
EP04024823A EP1528097B1 (en) 2003-10-29 2004-10-19 Method for reducing combustion chamber deposit flaking
ZA2004/08543A ZA200408543B (en) 2003-10-29 2004-10-21 Method for reducing combustion chamber deposit flaking
JP2004309792A JP2005133720A (en) 2003-10-29 2004-10-25 Method for reducing combustion chamber deposit peel-off
ARP040103895A AR046559A1 (en) 2003-10-29 2004-10-26 METHOD TO REDUCE THE DETACHMENT IN SCALES OF THE DEPOSITS OF THE COMBUSTION CHAMBER
RU2004131494/06A RU2283437C2 (en) 2003-10-29 2004-10-28 Method to reduce separation of deposits in combustion chamber and method to decrease exhaust when starting internal combustion engine from cold
BR0404762-1A BRPI0404762A (en) 2003-10-29 2004-10-28 Method for reducing flue deposit in the combustion chamber
KR1020040086425A KR20050040783A (en) 2003-10-29 2004-10-28 Method for reducing combustion chamber deposit flaking
SG200406302A SG111280A1 (en) 2003-10-29 2004-10-28 Method for reducing combustion chamber deposit flaking
CN2010102753375A CN101914397A (en) 2003-10-29 2004-10-28 Reduce the method for combustion chamber deposit flaking
CNA2004100921718A CN1637120A (en) 2003-10-29 2004-10-28 Ways to Reduce Flaking of Combustion Chamber Deposits

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US10/696,618 US20050091913A1 (en) 2003-10-29 2003-10-29 Method for reducing combustion chamber deposit flaking

Publications (1)

Publication Number Publication Date
US20050091913A1 true US20050091913A1 (en) 2005-05-05

Family

ID=34423374

Family Applications (1)

Application Number Title Priority Date Filing Date
US10/696,618 Abandoned US20050091913A1 (en) 2003-10-29 2003-10-29 Method for reducing combustion chamber deposit flaking

Country Status (15)

Country Link
US (1) US20050091913A1 (en)
EP (1) EP1528097B1 (en)
JP (1) JP2005133720A (en)
KR (1) KR20050040783A (en)
CN (2) CN1637120A (en)
AR (1) AR046559A1 (en)
AT (1) ATE491012T1 (en)
AU (1) AU2004218620A1 (en)
BR (1) BRPI0404762A (en)
CA (2) CA2677761C (en)
DE (1) DE602004030408D1 (en)
MX (1) MXPA04010020A (en)
RU (1) RU2283437C2 (en)
SG (1) SG111280A1 (en)
ZA (1) ZA200408543B (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20070245621A1 (en) * 2006-04-20 2007-10-25 Malfer Dennis J Additives for minimizing injector fouling and valve deposits and their uses
US20080076685A1 (en) * 2006-09-22 2008-03-27 Ian Macpherson Additives and lubricant formulations for improved used oil combustion properties
US20100009617A1 (en) * 2006-02-07 2010-01-14 Airbus Deutschland Gmbh Aircraft Air Conditioning System With Cyclone Dischargers

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8715373B2 (en) * 2007-07-10 2014-05-06 Afton Chemical Corporation Fuel composition comprising a nitrogen-containing compound
CN103965978A (en) * 2014-05-09 2014-08-06 陕西禾合化工科技有限公司 Transition metal gasoline antiknock agent

Citations (61)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2086775A (en) * 1936-07-13 1937-07-13 Leo Corp Method of operating an internal combustion engine
US2151432A (en) * 1937-07-03 1939-03-21 Leo Corp Method of operating internal combustion engines
US2818417A (en) * 1955-07-11 1957-12-31 Ethyl Corp Cyclomatic compounds
US2844447A (en) * 1953-12-29 1958-07-22 Standard Oil Co Gasoline fuel compositions
US3127351A (en) * 1964-03-31 Xxvii
US3179506A (en) * 1962-05-02 1965-04-20 Shell Oil Co Gasoline composition
US3442631A (en) * 1967-09-28 1969-05-06 Ethyl Corp Jet engine deposit modification
US4036605A (en) * 1971-09-01 1977-07-19 Gulf Research & Development Company Chelates of cerium (IV), their preparation and gasoline containing said chelates
US4104036A (en) * 1976-03-08 1978-08-01 Atlantic Richfield Company Iron-containing motor fuel compositions and method for using same
US4139349A (en) * 1977-09-21 1979-02-13 E. I. Du Pont De Nemours & Co. Fuel compositions containing synergistic mixtures of iron and manganese antiknock compounds
US4175927A (en) * 1978-03-27 1979-11-27 Ethyl Corporation Fuel compositions for reducing hydrocarbon emissions
US4191536A (en) * 1978-07-24 1980-03-04 Ethyl Corporation Fuel compositions for reducing combustion chamber deposits and hydrocarbon emissions of internal combustion engines
US4266946A (en) * 1980-04-28 1981-05-12 Ethyl Corporation Gasoline containing exhaust emission reducing additives
US4317657A (en) * 1978-03-27 1982-03-02 Ethyl Corporation Gasoline additive fluids to reduce hydrocarbon emissions
US4390345A (en) * 1980-11-17 1983-06-28 Somorjai Gabor A Fuel compositions and additive mixtures for reducing hydrocarbon emissions
US4474580A (en) * 1982-03-16 1984-10-02 Mackenzie Chemical Works, Inc. Combustion fuel additives comprising metal enolates
US4568357A (en) * 1984-12-24 1986-02-04 General Motors Corporation Diesel fuel comprising cerium and manganese additives for improved trap regenerability
US4588416A (en) * 1985-09-20 1986-05-13 Ethyl Corporation Fuel compositions
US4664677A (en) * 1983-10-05 1987-05-12 The Lubrizol Corporation Manganese and copper containing compositions
US4670020A (en) * 1984-12-24 1987-06-02 Ford Motor Company Carbon ignition temperature depressing agent and method of regenerating an automotive particulate trap utilizing said agent
US4674447A (en) * 1980-05-27 1987-06-23 Davis Robert E Prevention of fouling in internal combustion engines and their exhaust systems and improved gasoline compositions
US4690687A (en) * 1985-08-16 1987-09-01 The Lubrizol Corporation Fuel products comprising a lead scavenger
US4804388A (en) * 1987-10-02 1989-02-14 Ira Kukin Combustion control by addition of manganese and magnesium in specific amounts
US4891050A (en) * 1985-11-08 1990-01-02 Fuel Tech, Inc. Gasoline additives and gasoline containing soluble platinum group metal compounds and use in internal combustion engines
US4908045A (en) * 1988-12-23 1990-03-13 Velino Ventures, Inc. Engine cleaning additives for diesel fuel
US4946609A (en) * 1988-03-19 1990-08-07 Veba Oel Aktiengesellschaft Engine lubricating oil for diesel engines and process for operating a diesel engine
US4955331A (en) * 1988-01-23 1990-09-11 Vebe Oel Aktiengesellschaft Process for the operation of an Otto engine
US5034020A (en) * 1988-12-28 1991-07-23 Platinum Plus, Inc. Method for catalyzing fuel for powering internal combustion engines
US5113803A (en) * 1991-04-01 1992-05-19 Ethyl Petroleum Additives, Inc. Reduction of Nox emissions from gasoline engines
US5340369A (en) * 1991-05-13 1994-08-23 The Lubrizol Corporation Diesel fuels containing organometallic complexes
US5376154A (en) * 1991-05-13 1994-12-27 The Lubrizol Corporation Low-sulfur diesel fuels containing organometallic complexes
US5401280A (en) * 1992-10-14 1995-03-28 Nippon Oil Co., Ltd. Lead-free, high-octane gasoline
US5501714A (en) * 1988-12-28 1996-03-26 Platinum Plus, Inc. Operation of diesel engines with reduced particulate emission by utilization of platinum group metal fuel additive and pass-through catalytic oxidizer
US5551957A (en) * 1992-05-06 1996-09-03 Ethyl Corporation Compostions for control of induction system deposits
US5584894A (en) * 1992-07-22 1996-12-17 Platinum Plus, Inc. Reduction of nitrogen oxides emissions from vehicular diesel engines
US5599357A (en) * 1990-07-13 1997-02-04 Ehtyl Corporation Method of operating a refinery to reduce atmospheric pollution
US5679116A (en) * 1992-05-06 1997-10-21 Ethyl Corporation Compositions for control of induction system deposits
US5732548A (en) * 1994-10-07 1998-03-31 Platinum Plus, Inc. Method for reducing harmful emissions from two-stroke engines
US5758496A (en) * 1992-09-28 1998-06-02 Ford Global Technologies, Inc. Particulate and exhaust gas emission control system
US5809774A (en) * 1996-11-19 1998-09-22 Clean Diesel Technologies, Inc. System for fueling and feeding chemicals to internal combustion engines for NOx reduction
US5809775A (en) * 1997-04-02 1998-09-22 Clean Diesel Technologies, Inc. Reducing NOx emissions from an engine by selective catalytic reduction utilizing solid reagents
US5813224A (en) * 1993-07-06 1998-09-29 Ford Global Technologies, Inc. Method and apparatus for reducing NOx in the exhaust streams of internal combustion engines
US5912190A (en) * 1995-04-24 1999-06-15 The Associated Octel Company Limited Synergistic process for improving combustion
US5919276A (en) * 1997-02-07 1999-07-06 Ethyl Petroleum Additives Limited Use of mixed alkaline earth-alkali metal systems as emissions reducing agents in compression ignition engines
US5924280A (en) * 1997-04-04 1999-07-20 Clean Diesel Technologies, Inc. Reducing NOx emissions from an engine while maximizing fuel economy
US5928392A (en) * 1996-05-14 1999-07-27 Ethyl Corporation Enhanced combustion of hydrocarbonaceous burner fuels
US5944858A (en) * 1990-09-20 1999-08-31 Ethyl Petroleum Additives, Ltd. Hydrocarbonaceous fuel compositions and additives therefor
US5953906A (en) * 1995-02-10 1999-09-21 Gamel; Florian Exhaust gas purification device for internal combustion engines
US5976475A (en) * 1997-04-02 1999-11-02 Clean Diesel Technologies, Inc. Reducing NOx emissions from an engine by temperature-controlled urea injection for selective catalytic reduction
US6003303A (en) * 1993-01-11 1999-12-21 Clean Diesel Technologies, Inc. Methods for reducing harmful emissions from a diesel engine
US6023928A (en) * 1997-04-17 2000-02-15 Clean Diesel Technologies, Inc. Method for reducing emissions from a diesel engine
US6039772A (en) * 1984-10-09 2000-03-21 Orr; William C. Non leaded fuel composition
US6051040A (en) * 1988-12-28 2000-04-18 Clean Diesel Technologies, Inc. Method for reducing emissions of NOx and particulates from a diesel engine
US6056792A (en) * 1995-04-24 2000-05-02 The Associated Octel Company Limited combustion
US6152972A (en) * 1993-03-29 2000-11-28 Blue Planet Technologies Co., L.P. Gasoline additives for catalytic control of emissions from combustion engines
US6193767B1 (en) * 1999-09-28 2001-02-27 The Lubrizol Corporation Fuel additives and fuel compositions comprising said fuel additives
US6200358B1 (en) * 1998-04-24 2001-03-13 Daimlerchrysler Ag Additive for a fuel to neutralize sulfur dioxide and/or sulfur trioxide in the exhaust gases
US6206685B1 (en) * 1999-08-31 2001-03-27 Ge Energy And Environmental Research Corporation Method for reducing NOx in combustion flue gas using metal-containing additives
US6361754B1 (en) * 1997-03-27 2002-03-26 Clean Diesel Technologies, Inc. Reducing no emissions from an engine by on-demand generation of ammonia for selective catalytic reduction
US20020112466A1 (en) * 2000-12-12 2002-08-22 Roos Joseph W. Lean burn emissions system protectant composition and method
US20030097783A1 (en) * 2001-03-22 2003-05-29 Jordan Frederick L. Method and composition for using organic, plant-derived, oil-extracted materials in gasolines for reduced emissions

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB787374A (en) * 1956-01-12 1957-12-04 Ethyl Corp Antiknock compounds
NL248043A (en) * 1959-03-16 1900-01-01
CA2045706C (en) * 1990-07-13 2002-09-17 Thomas Albert Leeper Gasoline engine fuels of enhanced properties
GB9027389D0 (en) * 1990-12-18 1991-02-06 Shell Int Research Gasoline composition
RU2023196C1 (en) * 1991-02-12 1994-11-15 Казанский государственный технический университет им.А.Н.Туполева Internal combustion engine
US5203879A (en) * 1992-09-01 1993-04-20 Texaco Inc. Fuel composition
RU2064965C1 (en) * 1994-11-04 1996-08-10 Валерий Михайлович Фурсов Multi-functional additive agent to gasoline
US5873917A (en) * 1997-05-16 1999-02-23 The Lubrizol Corporation Fuel additive compositions containing polyether alcohol and hydrocarbylphenol
RU2188329C1 (en) * 2001-06-13 2002-08-27 Единархов Александр Станиславович Versalite fuel additive for internal combustion engine

Patent Citations (63)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3127351A (en) * 1964-03-31 Xxvii
US2086775A (en) * 1936-07-13 1937-07-13 Leo Corp Method of operating an internal combustion engine
US2151432A (en) * 1937-07-03 1939-03-21 Leo Corp Method of operating internal combustion engines
US2844447A (en) * 1953-12-29 1958-07-22 Standard Oil Co Gasoline fuel compositions
US2818417A (en) * 1955-07-11 1957-12-31 Ethyl Corp Cyclomatic compounds
US3179506A (en) * 1962-05-02 1965-04-20 Shell Oil Co Gasoline composition
US3442631A (en) * 1967-09-28 1969-05-06 Ethyl Corp Jet engine deposit modification
US4036605A (en) * 1971-09-01 1977-07-19 Gulf Research & Development Company Chelates of cerium (IV), their preparation and gasoline containing said chelates
US4104036A (en) * 1976-03-08 1978-08-01 Atlantic Richfield Company Iron-containing motor fuel compositions and method for using same
US4139349A (en) * 1977-09-21 1979-02-13 E. I. Du Pont De Nemours & Co. Fuel compositions containing synergistic mixtures of iron and manganese antiknock compounds
US4175927A (en) * 1978-03-27 1979-11-27 Ethyl Corporation Fuel compositions for reducing hydrocarbon emissions
US4317657A (en) * 1978-03-27 1982-03-02 Ethyl Corporation Gasoline additive fluids to reduce hydrocarbon emissions
US4191536A (en) * 1978-07-24 1980-03-04 Ethyl Corporation Fuel compositions for reducing combustion chamber deposits and hydrocarbon emissions of internal combustion engines
US4266946A (en) * 1980-04-28 1981-05-12 Ethyl Corporation Gasoline containing exhaust emission reducing additives
US4674447A (en) * 1980-05-27 1987-06-23 Davis Robert E Prevention of fouling in internal combustion engines and their exhaust systems and improved gasoline compositions
US4390345A (en) * 1980-11-17 1983-06-28 Somorjai Gabor A Fuel compositions and additive mixtures for reducing hydrocarbon emissions
US4474580A (en) * 1982-03-16 1984-10-02 Mackenzie Chemical Works, Inc. Combustion fuel additives comprising metal enolates
US4664677A (en) * 1983-10-05 1987-05-12 The Lubrizol Corporation Manganese and copper containing compositions
US6039772A (en) * 1984-10-09 2000-03-21 Orr; William C. Non leaded fuel composition
US4568357A (en) * 1984-12-24 1986-02-04 General Motors Corporation Diesel fuel comprising cerium and manganese additives for improved trap regenerability
US4670020A (en) * 1984-12-24 1987-06-02 Ford Motor Company Carbon ignition temperature depressing agent and method of regenerating an automotive particulate trap utilizing said agent
US4690687A (en) * 1985-08-16 1987-09-01 The Lubrizol Corporation Fuel products comprising a lead scavenger
US4588416A (en) * 1985-09-20 1986-05-13 Ethyl Corporation Fuel compositions
US4891050A (en) * 1985-11-08 1990-01-02 Fuel Tech, Inc. Gasoline additives and gasoline containing soluble platinum group metal compounds and use in internal combustion engines
US4804388A (en) * 1987-10-02 1989-02-14 Ira Kukin Combustion control by addition of manganese and magnesium in specific amounts
US4955331A (en) * 1988-01-23 1990-09-11 Vebe Oel Aktiengesellschaft Process for the operation of an Otto engine
US4946609A (en) * 1988-03-19 1990-08-07 Veba Oel Aktiengesellschaft Engine lubricating oil for diesel engines and process for operating a diesel engine
US4908045A (en) * 1988-12-23 1990-03-13 Velino Ventures, Inc. Engine cleaning additives for diesel fuel
US5034020A (en) * 1988-12-28 1991-07-23 Platinum Plus, Inc. Method for catalyzing fuel for powering internal combustion engines
US6051040A (en) * 1988-12-28 2000-04-18 Clean Diesel Technologies, Inc. Method for reducing emissions of NOx and particulates from a diesel engine
US5501714A (en) * 1988-12-28 1996-03-26 Platinum Plus, Inc. Operation of diesel engines with reduced particulate emission by utilization of platinum group metal fuel additive and pass-through catalytic oxidizer
US5599357A (en) * 1990-07-13 1997-02-04 Ehtyl Corporation Method of operating a refinery to reduce atmospheric pollution
US5944858A (en) * 1990-09-20 1999-08-31 Ethyl Petroleum Additives, Ltd. Hydrocarbonaceous fuel compositions and additives therefor
US5113803A (en) * 1991-04-01 1992-05-19 Ethyl Petroleum Additives, Inc. Reduction of Nox emissions from gasoline engines
US5376154A (en) * 1991-05-13 1994-12-27 The Lubrizol Corporation Low-sulfur diesel fuels containing organometallic complexes
US5340369A (en) * 1991-05-13 1994-08-23 The Lubrizol Corporation Diesel fuels containing organometallic complexes
US5551957A (en) * 1992-05-06 1996-09-03 Ethyl Corporation Compostions for control of induction system deposits
US5679116A (en) * 1992-05-06 1997-10-21 Ethyl Corporation Compositions for control of induction system deposits
US5584894A (en) * 1992-07-22 1996-12-17 Platinum Plus, Inc. Reduction of nitrogen oxides emissions from vehicular diesel engines
US5758496A (en) * 1992-09-28 1998-06-02 Ford Global Technologies, Inc. Particulate and exhaust gas emission control system
US5401280A (en) * 1992-10-14 1995-03-28 Nippon Oil Co., Ltd. Lead-free, high-octane gasoline
US6003303A (en) * 1993-01-11 1999-12-21 Clean Diesel Technologies, Inc. Methods for reducing harmful emissions from a diesel engine
US6152972A (en) * 1993-03-29 2000-11-28 Blue Planet Technologies Co., L.P. Gasoline additives for catalytic control of emissions from combustion engines
US5813224A (en) * 1993-07-06 1998-09-29 Ford Global Technologies, Inc. Method and apparatus for reducing NOx in the exhaust streams of internal combustion engines
US5732548A (en) * 1994-10-07 1998-03-31 Platinum Plus, Inc. Method for reducing harmful emissions from two-stroke engines
US5819529A (en) * 1994-10-07 1998-10-13 Clean Diesel Technologies, Inc. Method for reducing emissions from two-stroke engines
US5953906A (en) * 1995-02-10 1999-09-21 Gamel; Florian Exhaust gas purification device for internal combustion engines
US5912190A (en) * 1995-04-24 1999-06-15 The Associated Octel Company Limited Synergistic process for improving combustion
US6056792A (en) * 1995-04-24 2000-05-02 The Associated Octel Company Limited combustion
US5928392A (en) * 1996-05-14 1999-07-27 Ethyl Corporation Enhanced combustion of hydrocarbonaceous burner fuels
US5809774A (en) * 1996-11-19 1998-09-22 Clean Diesel Technologies, Inc. System for fueling and feeding chemicals to internal combustion engines for NOx reduction
US5919276A (en) * 1997-02-07 1999-07-06 Ethyl Petroleum Additives Limited Use of mixed alkaline earth-alkali metal systems as emissions reducing agents in compression ignition engines
US6361754B1 (en) * 1997-03-27 2002-03-26 Clean Diesel Technologies, Inc. Reducing no emissions from an engine by on-demand generation of ammonia for selective catalytic reduction
US5976475A (en) * 1997-04-02 1999-11-02 Clean Diesel Technologies, Inc. Reducing NOx emissions from an engine by temperature-controlled urea injection for selective catalytic reduction
US5809775A (en) * 1997-04-02 1998-09-22 Clean Diesel Technologies, Inc. Reducing NOx emissions from an engine by selective catalytic reduction utilizing solid reagents
US5924280A (en) * 1997-04-04 1999-07-20 Clean Diesel Technologies, Inc. Reducing NOx emissions from an engine while maximizing fuel economy
US6023928A (en) * 1997-04-17 2000-02-15 Clean Diesel Technologies, Inc. Method for reducing emissions from a diesel engine
US6200358B1 (en) * 1998-04-24 2001-03-13 Daimlerchrysler Ag Additive for a fuel to neutralize sulfur dioxide and/or sulfur trioxide in the exhaust gases
US6206685B1 (en) * 1999-08-31 2001-03-27 Ge Energy And Environmental Research Corporation Method for reducing NOx in combustion flue gas using metal-containing additives
US6193767B1 (en) * 1999-09-28 2001-02-27 The Lubrizol Corporation Fuel additives and fuel compositions comprising said fuel additives
US20020112466A1 (en) * 2000-12-12 2002-08-22 Roos Joseph W. Lean burn emissions system protectant composition and method
US20030177758A1 (en) * 2000-12-12 2003-09-25 Roos Joseph W. Lean burn emissions system protectant composition and method
US20030097783A1 (en) * 2001-03-22 2003-05-29 Jordan Frederick L. Method and composition for using organic, plant-derived, oil-extracted materials in gasolines for reduced emissions

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100009617A1 (en) * 2006-02-07 2010-01-14 Airbus Deutschland Gmbh Aircraft Air Conditioning System With Cyclone Dischargers
US8342921B2 (en) 2006-02-07 2013-01-01 Airbus Deutschland Gmbh Aircraft air conditioning system with cyclone dischargers
US20070245621A1 (en) * 2006-04-20 2007-10-25 Malfer Dennis J Additives for minimizing injector fouling and valve deposits and their uses
US20080076685A1 (en) * 2006-09-22 2008-03-27 Ian Macpherson Additives and lubricant formulations for improved used oil combustion properties
SG141290A1 (en) * 2006-09-22 2008-04-28 Afton Chemical Corp Additives and lubricant formulations for improved used oil combustion properties
US7780746B2 (en) 2006-09-22 2010-08-24 Afton Chemical Corporation Additives and lubricant formulations for improved used oil combustion properties

Also Published As

Publication number Publication date
CN1637120A (en) 2005-07-13
ZA200408543B (en) 2005-09-28
CA2482735A1 (en) 2005-04-29
ATE491012T1 (en) 2010-12-15
EP1528097B1 (en) 2010-12-08
DE602004030408D1 (en) 2011-01-20
MXPA04010020A (en) 2005-05-03
CA2677761C (en) 2011-09-13
KR20050040783A (en) 2005-05-03
CN101914397A (en) 2010-12-15
EP1528097A2 (en) 2005-05-04
AU2004218620A1 (en) 2005-05-19
EP1528097A3 (en) 2005-07-13
JP2005133720A (en) 2005-05-26
RU2283437C2 (en) 2006-09-10
SG111280A1 (en) 2005-05-30
CA2677761A1 (en) 2005-04-29
BRPI0404762A (en) 2005-06-28
AR046559A1 (en) 2005-12-14
CA2482735C (en) 2009-11-24
RU2004131494A (en) 2006-05-10

Similar Documents

Publication Publication Date Title
TW302419B (en)
US8852299B2 (en) Fuel composition
RU2263135C2 (en) Multifunctional additive for the motor fuel
RU2296152C2 (en) Method of enhancing operation of diesel fuel combustion systems
CA2677761C (en) Method for reducing cold start emissions
Danilov Fuel additives: evolution and use in 1996-2000
JP3841905B2 (en) Unleaded gasoline composition
JP2004091657A (en) Fuel for homogeneous charge compression self-ignition engine
Tupa et al. Gasoline and diesel fuel additives for performance/distribution/quality
US8852298B2 (en) Fuel composition containing iron and manganese to reduce spark plug fouling
JP2004091659A (en) Fuel for premixed compressed self-ignition type engine
CN102203224B (en) Improvement in or relating to fuel additive compositions
Tupa et al. Gasoline and diesel fuel additives for performance/distribution quality-II
CN102127471A (en) Ether-based fuel
JP2004091660A (en) Fuel for homogeneous charge compression self-ignition engine
JP2005042020A (en) Fuel for premixed compression self-ignition engines
JP2004091667A (en) Fuel for homogeneous charge compression self-ignition engine
JP2004091662A (en) Fuel for homogeneous charge compression self-ignition engine
FI4065671T3 (en) Use of alkyl phenol compounds as detergent additives for petrols
JP5436849B2 (en) Fuel oil composition for premixed compression ignition engines
JP2004091664A (en) Fuel for homogeneous charge compression self-ignition engine
JP2004091663A (en) Fuel for homogeneous charge compression self-ignition engine
JP2004091658A (en) Fuel for homogeneous charge compression self-ignition engine
EP1054051A1 (en) Diesel fuel compositions containing tertiary alkyl primary amines
JPH06192208A (en) Allophanic acid ester, its preparation and fuel composition for car containing it

Legal Events

Date Code Title Description
AS Assignment

Owner name: ETHYL PETROLEUM ADDITIVES, INC., VIRGINIA

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:ARADI, ALLEN A.;SMITH, JAMES B.;REEL/FRAME:014652/0990

Effective date: 20031024

AS Assignment

Owner name: SUNTRUST BANK, AS ADMINISTRATIVE AGENT, GEORGIA

Free format text: SECURITY AGREEMENT;ASSIGNOR:ETHYL PETROLEUM ADDITIVES, INC.;REEL/FRAME:014782/0317

Effective date: 20040618

AS Assignment

Owner name: AFTON CHEMICAL CORPORATION, VIRGINIA

Free format text: CHANGE OF NAME;ASSIGNOR:ETHYL PETROLEUM ADDITIVES, INC.;REEL/FRAME:015918/0557

Effective date: 20040701

AS Assignment

Owner name: SUNTRUST BANK,VIRGINIA

Free format text: SECURITY AGREEMENT;ASSIGNOR:AFTON CHEMICAL CORPORATION;REEL/FRAME:018883/0865

Effective date: 20061221

Owner name: SUNTRUST BANK, VIRGINIA

Free format text: SECURITY AGREEMENT;ASSIGNOR:AFTON CHEMICAL CORPORATION;REEL/FRAME:018883/0865

Effective date: 20061221

STCB Information on status: application discontinuation

Free format text: ABANDONED -- AFTER EXAMINER'S ANSWER OR BOARD OF APPEALS DECISION

AS Assignment

Owner name: AFTON CHEMICAL CORPORATION, VIRGINIA

Free format text: RELEASE BY SECURED PARTY;ASSIGNOR:SUNTRUST BANK;REEL/FRAME:026707/0563

Effective date: 20110513