CA2423859A1 - Low-emissions diesel fuel emulsions - Google Patents
Low-emissions diesel fuel emulsions Download PDFInfo
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- CA2423859A1 CA2423859A1 CA002423859A CA2423859A CA2423859A1 CA 2423859 A1 CA2423859 A1 CA 2423859A1 CA 002423859 A CA002423859 A CA 002423859A CA 2423859 A CA2423859 A CA 2423859A CA 2423859 A1 CA2423859 A1 CA 2423859A1
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/08—Use of additives to fuels or fires for particular purposes for improving lubricity; for reducing wear
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
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- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/188—Carboxylic acids; metal salts thereof
- C10L1/1881—Carboxylic acids; metal salts thereof carboxylic group attached to an aliphatic carbon atom
- C10L1/1883—Carboxylic acids; metal salts thereof carboxylic group attached to an aliphatic carbon atom polycarboxylic acid
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- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
- C10L1/328—Oil emulsions containing water or any other hydrophilic phase
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L10/00—Use of additives to fuels or fires for particular purposes
- C10L10/02—Use of additives to fuels or fires for particular purposes for reducing smoke development
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- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/12—Inorganic compounds
- C10L1/1233—Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof
- C10L1/125—Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof water
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- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/1814—Chelates
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/188—Carboxylic acids; metal salts thereof
- C10L1/1881—Carboxylic acids; metal salts thereof carboxylic group attached to an aliphatic carbon atom
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/188—Carboxylic acids; metal salts thereof
- C10L1/1886—Carboxylic acids; metal salts thereof naphthenic acid
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/188—Carboxylic acids; metal salts thereof
- C10L1/1888—Carboxylic acids; metal salts thereof tall oil
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/188—Carboxylic acids; metal salts thereof
- C10L1/189—Carboxylic acids; metal salts thereof having at least one carboxyl group bound to an aromatic carbon atom
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/22—Organic compounds containing nitrogen
- C10L1/234—Macromolecular compounds
- C10L1/238—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
- C10L1/2383—Polyamines or polyimines, or derivatives thereof (poly)amines and imines; derivatives thereof (substituted by a macromolecular group containing 30C)
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/30—Organic compounds compounds not mentioned before (complexes)
- C10L1/301—Organic compounds compounds not mentioned before (complexes) derived from metals
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
- C10L1/10—Liquid carbonaceous fuels containing additives
- C10L1/14—Organic compounds
- C10L1/30—Organic compounds compounds not mentioned before (complexes)
- C10L1/305—Organic compounds compounds not mentioned before (complexes) organo-metallic compounds (containing a metal to carbon bond)
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2430/00—Influencing exhaust purification, e.g. starting of catalytic reaction, filter regeneration, or the like, by controlling engine operating characteristics
- F01N2430/04—Influencing exhaust purification, e.g. starting of catalytic reaction, filter regeneration, or the like, by controlling engine operating characteristics by adding non-fuel substances to combustion air or fuel, e.g. additives
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/02—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust
- F01N3/021—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters
- F01N3/023—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for cooling, or for removing solid constituents of, exhaust by means of filters using means for regenerating the filters, e.g. by burning trapped particles
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Abstract
A low-emissions diesel fuel comprises fungible aviation kerosene emulsified with from 1 to 30 % water, and preferably contains 50-300 ppm detergent and 25- 500 ppm lubricity additive. Improved results can be achieved by also employi ng a fuel-soluble platinium group compound, such as 0.1-2.0 ppm platinium COD a nd a fuel-soluble cerium compound, such as 5-20 ppm cerium oleate. A method of reducing the emissions of pollutants from a diesel engine, comprising runnin g the engine on a fuel as defined. The method is improved by also employing another pollution-reducing technique selected from timing changes, exhaust g as recirculation, oxidation catalysts, lean NOx catalysts and particulate filte rs for enhanced emissions control,
Description
LOW-EMISSIONS DIESEL FUEL EMULSIONS
Background Of The Invention The invention concerns a new low-emissions diesel fuel based on an emulsion of a base fuel designed for use in jet engines and modified for use in diesel engines, especially of the type used to power buses in metropolitan areas where emissions are of special concern.
Efforts are being made in many jurisdictions to reduce the emissions of regulated pollutants like carbon monoxide, nitrogen oxides (NOX) and particulates.
The technologies have included those that modify the combustion conditions and fuels, known as primary measures, and those that treat the exhaust after combustion, known as secondary measures. When effective primary measures are employed, the secondary measures can still be employed to achieve further reductions.
There is a need for a new low-emissions fuel for use in diesel engines to reduce emissions of one or more regulated pollutants.
Summary Of The Invention The invention provides a new low-emissions fuel for use in diesel engines and a method of reducing pollutant emissions from diesel engines. The diesel fuel of the invention is in the form of an emulsion and its formulation and use in diesel engines are described below.
Many of the preferred aspects of the invention are described below. Equivalent compositions are contemplated.
Background Of The Invention The invention concerns a new low-emissions diesel fuel based on an emulsion of a base fuel designed for use in jet engines and modified for use in diesel engines, especially of the type used to power buses in metropolitan areas where emissions are of special concern.
Efforts are being made in many jurisdictions to reduce the emissions of regulated pollutants like carbon monoxide, nitrogen oxides (NOX) and particulates.
The technologies have included those that modify the combustion conditions and fuels, known as primary measures, and those that treat the exhaust after combustion, known as secondary measures. When effective primary measures are employed, the secondary measures can still be employed to achieve further reductions.
There is a need for a new low-emissions fuel for use in diesel engines to reduce emissions of one or more regulated pollutants.
Summary Of The Invention The invention provides a new low-emissions fuel for use in diesel engines and a method of reducing pollutant emissions from diesel engines. The diesel fuel of the invention is in the form of an emulsion and its formulation and use in diesel engines are described below.
Many of the preferred aspects of the invention are described below. Equivalent compositions are contemplated.
Description Of The Invention The invention provides a new diesel fuel comprised of an emulsion of water and a base fuel comprising a lubricity additive and a detergent. It is surprising that although a platinum and/or cerium fuel additive can be employed, such is not essential to the achievement of surprisingly good emission reductions as compared to conventional diesel fuel and diesel fuel emulsions.
The preferred detergent comprises polyolefin amide alkyleneamine (about 65-80%) and the remainder petroleum distillate. Equivalents which have the same essential function can also be employed. One preferred form is available from Texaco as TFA-4690-C, at concentrations of from about 50 to 300 ppm, more narrowly 75 to 150 ppm, e.g., about 100ppm, for W hich they provide the following analysis:
Properties Method Typical Density @ 15°C D4052 0.91-0.94 Nitrogen Content, wt.% D5291 2.3-2.4 Flash, °C, minimum D93 62 TBN, mgKOH/g D2896 50-60 Kinematic Viscosity, cSt at 40°C D445 600-850 A preferred lubricity additive comprises tall oil fatty acids, available commercially as mixture of fatty acids including oleic, linoleic and the like.
Equivalents which have the same essential function can also be employed.
Dimer acids are high molecular weight dibasic acids produced by the dimerization of unsaturated fatty acids at mid-molecule and usually contain 21-carbons. Similarly, trimer acids contain three carboxyl groups and usually 54 carbons.
Dimer and trimer acids are generally made by a Diels Alder reaction. This usually involves the reaction of an unsaturated fatty acid with another polyunsaturated fatty acid--typically linoleic acid. Starting raw materials usually include tall oiI
fatty acids.
In addition, it is also known to form dimer and trimer acids by reacting acrylic acid with polyunsaturated fatty acids.
The preferred detergent comprises polyolefin amide alkyleneamine (about 65-80%) and the remainder petroleum distillate. Equivalents which have the same essential function can also be employed. One preferred form is available from Texaco as TFA-4690-C, at concentrations of from about 50 to 300 ppm, more narrowly 75 to 150 ppm, e.g., about 100ppm, for W hich they provide the following analysis:
Properties Method Typical Density @ 15°C D4052 0.91-0.94 Nitrogen Content, wt.% D5291 2.3-2.4 Flash, °C, minimum D93 62 TBN, mgKOH/g D2896 50-60 Kinematic Viscosity, cSt at 40°C D445 600-850 A preferred lubricity additive comprises tall oil fatty acids, available commercially as mixture of fatty acids including oleic, linoleic and the like.
Equivalents which have the same essential function can also be employed.
Dimer acids are high molecular weight dibasic acids produced by the dimerization of unsaturated fatty acids at mid-molecule and usually contain 21-carbons. Similarly, trimer acids contain three carboxyl groups and usually 54 carbons.
Dimer and trimer acids are generally made by a Diels Alder reaction. This usually involves the reaction of an unsaturated fatty acid with another polyunsaturated fatty acid--typically linoleic acid. Starting raw materials usually include tall oiI
fatty acids.
In addition, it is also known to form dimer and trimer acids by reacting acrylic acid with polyunsaturated fatty acids.
After the reaction, the product usually comprises a small amount of monomer units, dimer acid, trimer acid, and higher analogs. Where the product desired is primarily dimer acid (i.e., at least about 85% dimer acid), the reactant product is often merely referred to as dimer acid. However, the individual components can be separated to provide a more pure form of dimer acid or trimer acid by itself.
Suitable dimer acids for use in this invention include Westvaco Diacid 1550, commercially available from Westvaco Chemicals of Charleston Heights, S.C.; Unidyme 12 and Unidyme 14, commercially available from Union Camp Corporation of Dover, Ohio;
Empol 1022, corrunercially available from Hen~el Corporation of Cincinnati, Ohio;
and Hystrene 3695, commercially available from Witco Co. of Memphis, Tenn.
In addition, blends of dimer and trimer acids can also be used as the lubricity additive of the present invention. These blends can be formed by combining dimer and trimer acids, or can comprise the reaction product from the formation of the dimer acid, which can contain substantial amounts of trimer acid. Generally, blends comprise about 5% to about 80% dimer acid. Specific blends include a blend of about 75% dimer acid and about 25% trimer acid, commercially available as Hystrene 3675, , a blend of 40% dimer acid and 60% trimer acid, commercially available as Hystrene 5460, and a blend of about 60% dimer acid and about ~ 40% trimer acid, all commercially available from Witco Co. of Memphis, Tenn.
One preferred form of lubricity additive is available from Texaco as TFA-4769, at concentrations of from about 25 to 500 ppm, e.g., about 50-150 ppm, for which they provide the following analysis:
Properties Method Typical Specific Gravity, 60/60°F D1298 0.91 PoundslGallon, 60°F Calculated 7.54 Flash, °F, minimum D93 142 I~inematic Viscosity, cSt at 40°C D445 17.85 The base fuel comprises a commercially-available jet fuel. It can be purchased from Colonial Pipeline Company as "fungible aviation kerosene grade 55".
Equivalents which have the same essential function and those varying compositionally by up to 15 %, preferably by less than 5%, can also be employed. It is characterized by the following average analysis:
ASTM Test Parameter Method Value Cetane Number D-613 50.4 Hdrocarbon D-1319 Aromatics, vol% 15.3 Olefins, vol% . 1.8 Saturates, vol% 82.9 Flash Point (F) D-93 138 API Gravity D-4052 44.4 Specific Gravity 0.8045 Viscosity, 40C (cSt)D-445 1.46 Sulfur (weight %) D-2622 0.03341 ppm 334 Heat of Combustion, Gross (BTU/Pound) D-240 19,794.7 Net (BTU/Pound) 18,519.4 Pour Point (C) D-97 -48 Cloud Point (C) D-2500 -45 Cetane Ilidex (calculated)D-976 42 minimum, 48 test ' Lower sulfur forms of this formulation, as low as 5 to 30 ppm sulfur, can provide fiu-ther advantages and are included.
Simulated Distillation D-2887 (~C) IBP 119.7 156.7 167.2 173.8 180.8 194.3 203.6 215.3 226.2 235.7 250.2 265.1 276.3 FBP 304.7 The fuel as described above will be formulated as an emulsion of water-in-oil where the emulsion is made by inclusion of from 1 to 30% of an aqueous phase with 70-99% of the oil phase as previously defined. Surfactants, lubricity agents and/or corrosion inhibitors can be added as described in U. S. Patent No. 5,743,922 or as otherwise known in the art. An emulsion of water-in-oil typically provides about 1 NOX reduction for each 1 % water added. The new fuel improves the reductions in pollutants normally achieved with diesel fuel emulsions and its combination with other pollution control technologies will provide emissions reductions greater than either alone. The use of platinum group metal and/or cerium fuel-borne catalysts is optional, but can further enhance reductions. In one preferred form, the emulsion is prepared in the absence of such additives.
The fuel thus formed can be used to fuel a diesel engine with reduced emissions of pollutants, which can be further enhanced with the simultaneous use of engine timing changes, exhaust gas recirculation, oxidation catalysts, lean NOX
catalysts and/or particulate filters for enhanced emissions control.
The fuel can contain a fuel-soluble catalyst comprised of fuel-soluble platinum group metal compositions and/or cerium compositions. One or more of these optional additives can be employed in forms and amounts effective to deliver the catalytic metal in active form to the exhaust system of a diesel engine.
Among the specific cerium compounds are: cerium III acetylacetonate, cerium III napthenate, and cerium octoate and other soaps such as stearate, neodecanoate, and octoate (2-ethylhexoate). Many of the cerium compounds are trivalent compounds meeting the formula: Ce (OOCR)3 wherein R=hydrocarbon, preferably Cz to C22, and including aliphatic, alicyclic, aryl and alkylaryl. The cerium is preferred at concentrations of 2 to 20 ppm, more narrowly form 4 to 15 ppm, cerium w/v of fuel, i.e., weight of ceriinn metal in mg to volume of fuel in liters. Preferably, the cerium is supplied as cerium hydroxy oleate propionate complex (40% cerium by weight).
Preferred levels are toward the lower end of this range.
Any of the platinum group metal compositions, e.g., 1,5-cyclooctadiene platinum diphenyl (platinum COD), described in U.S. Pat. No. 4,891,050 to Bowers, et al., U.S. Pat. No. 5,034,020 to Epperly, et al., and U.S. Pat. No.
Suitable dimer acids for use in this invention include Westvaco Diacid 1550, commercially available from Westvaco Chemicals of Charleston Heights, S.C.; Unidyme 12 and Unidyme 14, commercially available from Union Camp Corporation of Dover, Ohio;
Empol 1022, corrunercially available from Hen~el Corporation of Cincinnati, Ohio;
and Hystrene 3695, commercially available from Witco Co. of Memphis, Tenn.
In addition, blends of dimer and trimer acids can also be used as the lubricity additive of the present invention. These blends can be formed by combining dimer and trimer acids, or can comprise the reaction product from the formation of the dimer acid, which can contain substantial amounts of trimer acid. Generally, blends comprise about 5% to about 80% dimer acid. Specific blends include a blend of about 75% dimer acid and about 25% trimer acid, commercially available as Hystrene 3675, , a blend of 40% dimer acid and 60% trimer acid, commercially available as Hystrene 5460, and a blend of about 60% dimer acid and about ~ 40% trimer acid, all commercially available from Witco Co. of Memphis, Tenn.
One preferred form of lubricity additive is available from Texaco as TFA-4769, at concentrations of from about 25 to 500 ppm, e.g., about 50-150 ppm, for which they provide the following analysis:
Properties Method Typical Specific Gravity, 60/60°F D1298 0.91 PoundslGallon, 60°F Calculated 7.54 Flash, °F, minimum D93 142 I~inematic Viscosity, cSt at 40°C D445 17.85 The base fuel comprises a commercially-available jet fuel. It can be purchased from Colonial Pipeline Company as "fungible aviation kerosene grade 55".
Equivalents which have the same essential function and those varying compositionally by up to 15 %, preferably by less than 5%, can also be employed. It is characterized by the following average analysis:
ASTM Test Parameter Method Value Cetane Number D-613 50.4 Hdrocarbon D-1319 Aromatics, vol% 15.3 Olefins, vol% . 1.8 Saturates, vol% 82.9 Flash Point (F) D-93 138 API Gravity D-4052 44.4 Specific Gravity 0.8045 Viscosity, 40C (cSt)D-445 1.46 Sulfur (weight %) D-2622 0.03341 ppm 334 Heat of Combustion, Gross (BTU/Pound) D-240 19,794.7 Net (BTU/Pound) 18,519.4 Pour Point (C) D-97 -48 Cloud Point (C) D-2500 -45 Cetane Ilidex (calculated)D-976 42 minimum, 48 test ' Lower sulfur forms of this formulation, as low as 5 to 30 ppm sulfur, can provide fiu-ther advantages and are included.
Simulated Distillation D-2887 (~C) IBP 119.7 156.7 167.2 173.8 180.8 194.3 203.6 215.3 226.2 235.7 250.2 265.1 276.3 FBP 304.7 The fuel as described above will be formulated as an emulsion of water-in-oil where the emulsion is made by inclusion of from 1 to 30% of an aqueous phase with 70-99% of the oil phase as previously defined. Surfactants, lubricity agents and/or corrosion inhibitors can be added as described in U. S. Patent No. 5,743,922 or as otherwise known in the art. An emulsion of water-in-oil typically provides about 1 NOX reduction for each 1 % water added. The new fuel improves the reductions in pollutants normally achieved with diesel fuel emulsions and its combination with other pollution control technologies will provide emissions reductions greater than either alone. The use of platinum group metal and/or cerium fuel-borne catalysts is optional, but can further enhance reductions. In one preferred form, the emulsion is prepared in the absence of such additives.
The fuel thus formed can be used to fuel a diesel engine with reduced emissions of pollutants, which can be further enhanced with the simultaneous use of engine timing changes, exhaust gas recirculation, oxidation catalysts, lean NOX
catalysts and/or particulate filters for enhanced emissions control.
The fuel can contain a fuel-soluble catalyst comprised of fuel-soluble platinum group metal compositions and/or cerium compositions. One or more of these optional additives can be employed in forms and amounts effective to deliver the catalytic metal in active form to the exhaust system of a diesel engine.
Among the specific cerium compounds are: cerium III acetylacetonate, cerium III napthenate, and cerium octoate and other soaps such as stearate, neodecanoate, and octoate (2-ethylhexoate). Many of the cerium compounds are trivalent compounds meeting the formula: Ce (OOCR)3 wherein R=hydrocarbon, preferably Cz to C22, and including aliphatic, alicyclic, aryl and alkylaryl. The cerium is preferred at concentrations of 2 to 20 ppm, more narrowly form 4 to 15 ppm, cerium w/v of fuel, i.e., weight of ceriinn metal in mg to volume of fuel in liters. Preferably, the cerium is supplied as cerium hydroxy oleate propionate complex (40% cerium by weight).
Preferred levels are toward the lower end of this range.
Any of the platinum group metal compositions, e.g., 1,5-cyclooctadiene platinum diphenyl (platinum COD), described in U.S. Pat. No. 4,891,050 to Bowers, et al., U.S. Pat. No. 5,034,020 to Epperly, et al., and U.S. Pat. No.
5,266,093 to Peter-Hoblyn, et al., can be employed as the platinum source. Other suitable platinum group metal catalyst compositions include commercially-available or easily-synthesized platinum group metal acetylacetonates, platinum group metal dibenzylidene acetonates, and fatty acid soaps of tetramine platinum metal complexes, e.g., tetramine platinum oleate. The platinum is preferred at concentrations of 0.1 -2.0 ppm, e.g., up to about 1.0 ppm platinum w/v of fuel. Preferred levels are toward the lower end of this range, e.g., 0.15 -0.5 ppm. Platinum COD is the preferred form of platinum fox addition to the fuel.
The term "diesel particulate filter" is meant to refer to those devices known in the art as exhaust gas filters that reduce particulate emissions by trapping a portion of the particulates within a complex internal structure. They must be regenerated or replaced as deposits will accumulate. The fuel borne catalyst described above, when used with the base fuel as also described - forming the fuel of the invention -enables very reduced emissions with enhanced filter operation.
The term "lean NOX catalysts" is meant to refer to those devices known in the art for catalytically reducing NOX emissions under lean fuel (oxygen-rich) conditions.
Suitable catalysts of this type are described in U. S. Patent No. 4,904,633 to Ohata , et al., which is hereby incorporated by reference in its entirety.
The term "diesel oxidation catalyst" is meant to refer to those devices known in the axt as exhaust gas treatment catalysts that reduce particulate, hydrocarbon and carbon monoxide emissions by causing contact with catalyzed surfaces in lieu of trapping particulates as done in the diesel particulate filters. The fuel borne catalyst described above, when used with the base fuel as also described - forming the fuel of the invention - enables very reduced emissions with enhanced oxidation catalyst operation.
Retarding engine timing, e.g., by from about 2 to about 6°, is a known procedure for reducing NOX, unfortunately it will by itself cause pollutant generation due to poor combustion. This tradeoff has been troubling the art since emissions control became important. It is an advantage of the invention, that both reduced NOX
and other pollutants can be achieved by employing the fuel of the invention in combination with one or more of the above techniques and/or exhaust gas recirculation wherein a portion of the exhaust gas is intermixed with combustion air.
The following Examples axe provided to further illustrate and explain a preferred form of the invention and are not to be taken as limiting in any regard.
Unless otherwise indicated, all paxts and percentages are by weight.
Example 1 This example describes the preparation of a low-emissions diesel fuel according to a preferred aspect of the invention. A fuel is blended using the Colonial Pipeline Company fungible aviation kerosene grade 55 analyzed above, with 100 ppm of the TFA 4690-C detergent, 150-250 ppm of the noted Texaco lubricity additive and 20% water by weight. The fuel was emulsified to obtain a water in oil emulsion which is used to fuel a diesel engine with reduced production of pollutants.
The above description is intended to enable the person skilled in the art to practice the invention. It is not intended to detail all of the possible modifications and variations which will become apparent to the skilled worker upon reading the description. It is intended, however, that all such modifications and variations be included within the scope of the invention which is seen in the above description and otherwise defined by the following claims. The claims are meant to cover the indicated elements and steps in any arrangement or sequence which is effective to meet the obj ectives intended for the invention, unless the context specifically indicates the contrary.
The term "diesel particulate filter" is meant to refer to those devices known in the art as exhaust gas filters that reduce particulate emissions by trapping a portion of the particulates within a complex internal structure. They must be regenerated or replaced as deposits will accumulate. The fuel borne catalyst described above, when used with the base fuel as also described - forming the fuel of the invention -enables very reduced emissions with enhanced filter operation.
The term "lean NOX catalysts" is meant to refer to those devices known in the art for catalytically reducing NOX emissions under lean fuel (oxygen-rich) conditions.
Suitable catalysts of this type are described in U. S. Patent No. 4,904,633 to Ohata , et al., which is hereby incorporated by reference in its entirety.
The term "diesel oxidation catalyst" is meant to refer to those devices known in the axt as exhaust gas treatment catalysts that reduce particulate, hydrocarbon and carbon monoxide emissions by causing contact with catalyzed surfaces in lieu of trapping particulates as done in the diesel particulate filters. The fuel borne catalyst described above, when used with the base fuel as also described - forming the fuel of the invention - enables very reduced emissions with enhanced oxidation catalyst operation.
Retarding engine timing, e.g., by from about 2 to about 6°, is a known procedure for reducing NOX, unfortunately it will by itself cause pollutant generation due to poor combustion. This tradeoff has been troubling the art since emissions control became important. It is an advantage of the invention, that both reduced NOX
and other pollutants can be achieved by employing the fuel of the invention in combination with one or more of the above techniques and/or exhaust gas recirculation wherein a portion of the exhaust gas is intermixed with combustion air.
The following Examples axe provided to further illustrate and explain a preferred form of the invention and are not to be taken as limiting in any regard.
Unless otherwise indicated, all paxts and percentages are by weight.
Example 1 This example describes the preparation of a low-emissions diesel fuel according to a preferred aspect of the invention. A fuel is blended using the Colonial Pipeline Company fungible aviation kerosene grade 55 analyzed above, with 100 ppm of the TFA 4690-C detergent, 150-250 ppm of the noted Texaco lubricity additive and 20% water by weight. The fuel was emulsified to obtain a water in oil emulsion which is used to fuel a diesel engine with reduced production of pollutants.
The above description is intended to enable the person skilled in the art to practice the invention. It is not intended to detail all of the possible modifications and variations which will become apparent to the skilled worker upon reading the description. It is intended, however, that all such modifications and variations be included within the scope of the invention which is seen in the above description and otherwise defined by the following claims. The claims are meant to cover the indicated elements and steps in any arrangement or sequence which is effective to meet the obj ectives intended for the invention, unless the context specifically indicates the contrary.
Claims (10)
1. A low-emissions diesel fuel comprising an emulsion of from 1 to 30% of an aqueous phase and 70-99% of an oil phase comprised of aviation grade kerosene, detergent and lubricity additive.
2. A low-emissions diesel fuel according to claim 1 formulated as an emulsion of water-in-oil where and contains 50-300 ppm detergent, 25-500 ppm lubricity additive.
3. A low-emissions diesel fuel according to claim 1 formulated as an emulsion of water-in-oil where and contains aviation kerosene grade 55.
4. A low-emissions fuel according to claim 1, further comprising platinum and/or cerium fuel additives.
5. A low-emissions diesel fuel according to claim 4 comprising fuel-soluble platinum composition and fuel-soluble cerium composition.
6. A low-emissions diesel fuel formulated as an emulsion of water-in-oil where the emulsion is made by inclusion of from 1 to 30% of an aqueous phase with 70-99%
of an oil phase comprising fungible aviation kerosene grade 55, 50-300 ppm detergent, 150-250 ppm lubricity additive and 0.1 -1.0 ppm platinum supplied as platinum COD and 2-15 ppm cerium supplied as cerium hydroxy oleate propionate complex.
of an oil phase comprising fungible aviation kerosene grade 55, 50-300 ppm detergent, 150-250 ppm lubricity additive and 0.1 -1.0 ppm platinum supplied as platinum COD and 2-15 ppm cerium supplied as cerium hydroxy oleate propionate complex.
7. A method of reducing the emissions of pollutants from a diesel engine, comprising running the engine on a fuel as defined in any of claims 1-7.
8. A method of reducing the emissions of pollutants from a diesel engine according to claim 7 wherein the method is improved by also employing another pollution-reducing technique selected from timing changes, exhaust gas recirculation, oxidation catalysts, lean NO x catalysts and particulate filters for enhanced emissions control.
9. A method of reducing the emissions of pollutants from a diesel engine, comprising running the engine on a fuel formulated as an emulsion of water-in-oil where the emulsion is made by inclusion of from 1 to 30% of an aqueous phase with 70-99% of an oil phase comprising fungible aviation kerosene grade 55, 50-300 ppm detergent, 150-250 ppm lubricity additive fuel-soluble platinum composition and fuel-soluble cerium composition, and also including also employing another pollution-reducing technique selected from timing changes, exhaust gas recirculation, oxidation catalysts, lean NO x catalysts and particulate filters for enhanced emissions control.
10. A method of reducing the emissions of pollutants from a diesel engine according to claim 9 which contains 0.1 - 2.0 ppm platinum supplied as platinum COD and 2 - 15 ppm cerium supplied as cerium hydroxy oleate propionate complex
Applications Claiming Priority (3)
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US23613600P | 2000-09-28 | 2000-09-28 | |
US60/236,136 | 2000-09-28 | ||
PCT/US2001/030606 WO2002026918A1 (en) | 2000-09-28 | 2001-09-28 | Low-emissions diesel fuel emulsions |
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CA2423859A1 true CA2423859A1 (en) | 2002-04-04 |
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CA002423859A Abandoned CA2423859A1 (en) | 2000-09-28 | 2001-09-28 | Low-emissions diesel fuel emulsions |
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US (1) | US20040098905A1 (en) |
EP (1) | EP1337608A4 (en) |
AU (1) | AU2001294915A1 (en) |
CA (1) | CA2423859A1 (en) |
WO (1) | WO2002026918A1 (en) |
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US20050188605A1 (en) * | 2000-08-01 | 2005-09-01 | Valentine James M. | Reduced-emissions combustion utilizing multiple-component metallic combustion catalyst |
US20050160663A1 (en) * | 2000-08-01 | 2005-07-28 | Valentine James M. | Cleaner burning diesel fuel |
US20030226312A1 (en) * | 2002-06-07 | 2003-12-11 | Roos Joseph W. | Aqueous additives in hydrocarbonaceous fuel combustion systems |
US7413583B2 (en) * | 2003-08-22 | 2008-08-19 | The Lubrizol Corporation | Emulsified fuels and engine oil synergy |
CN100413943C (en) * | 2005-01-21 | 2008-08-27 | 黄明忠 | Emusified fuel oil and preparation method |
DE102010054362A1 (en) | 2010-12-13 | 2012-06-14 | Lurgi Gmbh | Synthetic fuel composition, useful for the internal combustion in diesel engines and heating systems, preferably for operating diesel motors for vehicles, comprises specified range of hydrocarbon, where hydrocarbons are partially alkanes |
US10173700B2 (en) | 2013-01-07 | 2019-01-08 | Whitmore Manufacturing, Llc | Top of rail applicator and method of using the same |
US10960907B2 (en) | 2013-01-07 | 2021-03-30 | Whitmore Manufacturing, Llc | Top of rail applicator |
US9511355B2 (en) | 2013-11-26 | 2016-12-06 | Clean Diesel Technologies, Inc. (Cdti) | System and methods for using synergized PGM as a three-way catalyst |
US9511353B2 (en) | 2013-03-15 | 2016-12-06 | Clean Diesel Technologies, Inc. (Cdti) | Firing (calcination) process and method related to metallic substrates coated with ZPGM catalyst |
US9511350B2 (en) | 2013-05-10 | 2016-12-06 | Clean Diesel Technologies, Inc. (Cdti) | ZPGM Diesel Oxidation Catalysts and methods of making and using same |
US9771534B2 (en) | 2013-06-06 | 2017-09-26 | Clean Diesel Technologies, Inc. (Cdti) | Diesel exhaust treatment systems and methods |
US9545626B2 (en) | 2013-07-12 | 2017-01-17 | Clean Diesel Technologies, Inc. | Optimization of Zero-PGM washcoat and overcoat loadings on metallic substrate |
US9511358B2 (en) | 2013-11-26 | 2016-12-06 | Clean Diesel Technologies, Inc. | Spinel compositions and applications thereof |
US9604175B2 (en) | 2014-06-06 | 2017-03-28 | Clean Diesel Technologies, Inc. | Three-way catalyst systems including Nb—Zr—Al-mixed oxide supports, Ba—Pd, and Rh—Fe material compositions |
US9731279B2 (en) | 2014-10-30 | 2017-08-15 | Clean Diesel Technologies, Inc. | Thermal stability of copper-manganese spinel as Zero PGM catalyst for TWC application |
US9700841B2 (en) | 2015-03-13 | 2017-07-11 | Byd Company Limited | Synergized PGM close-coupled catalysts for TWC applications |
US9951706B2 (en) | 2015-04-21 | 2018-04-24 | Clean Diesel Technologies, Inc. | Calibration strategies to improve spinel mixed metal oxides catalytic converters |
US10533472B2 (en) | 2016-05-12 | 2020-01-14 | Cdti Advanced Materials, Inc. | Application of synergized-PGM with ultra-low PGM loadings as close-coupled three-way catalysts for internal combustion engines |
US9861964B1 (en) | 2016-12-13 | 2018-01-09 | Clean Diesel Technologies, Inc. | Enhanced catalytic activity at the stoichiometric condition of zero-PGM catalysts for TWC applications |
US10265684B2 (en) | 2017-05-04 | 2019-04-23 | Cdti Advanced Materials, Inc. | Highly active and thermally stable coated gasoline particulate filters |
CN112257551B (en) * | 2020-10-19 | 2021-09-10 | 北京市劳动保护科学研究所 | Method and system for identifying nitrogen oxide pollution source and determining emission |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
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US4696638A (en) * | 1986-07-07 | 1987-09-29 | Denherder Marvin J | Oil fuel combustion |
US5693106A (en) * | 1992-07-22 | 1997-12-02 | Platinum Plus, Inc. | Platinum metal fuel additive for water-containing fuels |
US5584894A (en) * | 1992-07-22 | 1996-12-17 | Platinum Plus, Inc. | Reduction of nitrogen oxides emissions from vehicular diesel engines |
US5284492A (en) * | 1991-10-01 | 1994-02-08 | Nalco Fuel Tech | Enhanced lubricity fuel oil emulsions |
GB2364713B (en) * | 1999-03-06 | 2003-08-27 | Pauline Abu-Jawdeh | Compositions for preparing water-in-fuel microemulsions |
EP1409617A1 (en) * | 2000-05-08 | 2004-04-21 | Clean Diesel Technologies Inc. | Low-emissions diesel fuel |
WO2002010317A1 (en) * | 2000-08-01 | 2002-02-07 | Clean Diesel Technologies, Inc. | Low-emissions diesel fuel blend |
-
2001
- 2001-09-28 EP EP01975605A patent/EP1337608A4/en not_active Withdrawn
- 2001-09-28 CA CA002423859A patent/CA2423859A1/en not_active Abandoned
- 2001-09-28 WO PCT/US2001/030606 patent/WO2002026918A1/en not_active Application Discontinuation
- 2001-09-28 AU AU2001294915A patent/AU2001294915A1/en not_active Abandoned
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2003
- 2003-03-28 US US10/401,367 patent/US20040098905A1/en not_active Abandoned
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EP1337608A1 (en) | 2003-08-27 |
WO2002026918A1 (en) | 2002-04-04 |
AU2001294915A1 (en) | 2002-04-08 |
US20040098905A1 (en) | 2004-05-27 |
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