US2655440A - Diesel fuel oil - Google Patents

Diesel fuel oil Download PDF

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US2655440A
US2655440A US95146A US9514649A US2655440A US 2655440 A US2655440 A US 2655440A US 95146 A US95146 A US 95146A US 9514649 A US9514649 A US 9514649A US 2655440 A US2655440 A US 2655440A
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fuel
oil
cetane
per cent
peroxide
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Maurice R Barusch
Robert Y Mixer
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California Research LLC
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/143Organic compounds mixtures of organic macromolecular compounds with organic non-macromolecular 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, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/1811Organic compounds containing oxygen peroxides; ozonides
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/198Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
    • C10L1/1985Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid polyethers, e.g. di- polygylcols and derivatives; ethers - esters
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/226Organic compounds containing nitrogen containing at least one nitrogen-to-nitrogen bond, e.g. azo compounds, azides, hydrazines
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/23Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/23Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites
    • C10L1/231Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites nitro compounds; nitrates; nitrites
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2406Organic compounds containing sulfur, selenium and/or tellurium mercaptans; hydrocarbon sulfides

Definitions

  • This invention relates to an improved diesel fuel oil, and more particularly to improved diesel fuel-oil compositions having high cetane numbers.
  • Diesel engines depend upon the heat developed by compressing a charge of air to ignite the fuel injected into the engine cylinder after the air is compressed.
  • a high compression ratio is necessary because most known diesel fuels require a relatively high compression ratio in order to ignite.
  • a factor of major importance in regard to the performance of a diesel fuel oil is the delay in ignition from the beginning of the injection of the fuel to the beginning of its combustion. This property is commonly termed the ignitiondelay characteristic of the fuel and may be expressed in terms of cetane numbers. If ignition delay is too long, the motor fuel will accumulate in the cylinder until it reaches ignition conditions and then will burn rapidly, causing a sudden pressure increase which may result in engine knocking. In addition, too long an ignition delay may result in a smoky exhaust, a decrease in en'- gine efliciency, and possibly crankcase-oil dilution.
  • An object of the present invention is to provide a diesel fuel-oil composition having a high cetane number that ignites readily and functions smoothly under operating conditions.
  • Another object of this invention is to provide a diesel fuel-oil composition that is readily adaptable for starting cold diesel engines.
  • Still another object of this invention is to provide a high octane number diesel fuel-oil composition whose base has a low cetane number.
  • a further object of this invention is to provide a diesel fuel-oil composition that may be used as a reference fuel for fuels having cetane numbers in excess of 100.
  • cetaneimproving materials In order to meet the increasing demand for diesel fuel oils having high octane numbers, various octane-improving materials have been added to the petroleum fuel oil base.
  • the use of cetaneimproving materials has also permitted the employment of base fuels having relatively low cetane numbers and has thereby increased, in many instances, the usefulness of middle-ofthe-barrel stock to the refiners.
  • the cetaneimproving materials have been generally of an additive or blend type. The characteristics and properties of these are described below.
  • the amount of a octane-improving additive added to a diesel fuel oil is in the range of about .001 per cent to about 10 per cent.
  • Suitable additives which may be employed as the cetane-improving additive are: alkyl nitrate and nitrites; nitroso compounds; di-azo compounds; di-sulfides; and hydrocarbon peroxides such as di-alkyl peroxides and alkyl hydroperoxides, including peroxides of the tertiary type and corresponding alicyclic peroxides, and acyl peroxides.
  • the alkyl peroxides and hydroperoxides include the following specific compounds: ethyl peroxide and hydroperoxide; isobutene peroxides and hydroperoxides; isopentene peroxides and hydroperoxides; 2-methylpentane peroxides and hydroperoxides; 2-ethyl butene peroxide and hydroperoxide; 2-methylpentane peroxides and hydroperoxides; 3-methylpentane peroxide and hydroperoxide; 2,3-dimethyl butane peroxide and hydroperoxide; and 2,4-dimethylbutane peroxide and hydroperoxide.
  • Peroxides of the di(tertiary alkyl) type include: di(tertiary butyl) peroxide; di (tertiary amyl) peroxide; di (21-"nethyl, 2-pentyl) peroxide; di(3-methyl,3-pentyl) peroxide; di(2-ethyl,2-butyl) peroxide; di(l-halo, 2-propyl) peroxide; di(1-halo,2-methyl,2-butyl) peroxide; di(1-halo,3-methyl,3-butyl) peroxide; di(Z halo, 3 -methyl,3 butyl) peroxide; di(lphenyl,1-methyl,1-propyl) peroxide, and di(lphenyl,2-methyl,2-propyl) peroxide.
  • Cyclic hydrocarbon peroxides include; cyclopentyl hydroperoxide; methylcyclopentyl hydroperoxides; the isomeric dimethylcyclopentyl hydroperoxides; ethylcyclopentyl peroxides; the isomeric diethylcyclopentyl hydroperoxides; the isomeric methylethylcyclopentyl hydroperoxides, cyclohexyl hydroperoxide, methylcyclohexyl hydroperoxides; the isomeric dimethylcyclohexyl hydroperoxides; ethylcyclohexyl hydroperoxides; the isomeric diethylcyclohexyl hydroperoxides; l-4-methyl isopropylcyclohexyl hydroperoxide; hydroperoxides of cyclopentane, cycloheptane, etc., andhigher molecular weight substituted cycloparafiins.
  • Peroxides especially suitable for the composition of our invention are non-benzenoid hydrocarbon peroxides which; include the aliphatic and alicyclic peroxides.
  • non-benzenoid peroxides is illustrated by the cetane-improving additive disclosed in Schultz et al. Patent No. 2,317,968 and is prepared by partially oxidizing a petroleum distillate rela-v tively free from asphaltic and resinous materials,
  • Patent to Denison et al., No. 2,521,698 discloses another especially desirable non-benzenoid hydrocarbon peroxide for. the composition of our invention which may be used as a cetane-improving material and that is prepared by subjecting a petroleum distillate having a boiling range between 200 and 450 and relatively free from asphaltic and resinous materials and from large proportions of aromatic ring compounds to a liquid-phase oxidation treatment with an oxygen-containing gas at a temperature within the range of 200 to 400 F. for a period of time, suiiicient to produce an oil having an oxygen factor higher than 250; contacting the resulting oxygenated oil with 0.1 to 0.75 pound of 50-90 per cent H2804 per gallon of oil at a temperature of 50 to 85 F.
  • blending agent as used herein and in the appended claims is a material which produces a cetane improvement in diesel fuel oils corresponding to the amount of blending agent added and the cetane number of the blending agent.
  • the amount of blending agent generally added to diesel fueloils is above about 5 per cent.
  • the aliphatic polyether blendin agents especially suitable for the composition of this invention are normally liquid oil-soluble aliphatic polyethers especially alkyl polyethers having a An example of these molecular weight .belowabout '700;'with; a;general formula:
  • R(OX) n-OR wherein R and R are like or unlike alkyl groups, X' islahydrocarbon group of the alkylene type having at least two carbon atoms, nis an integer, and when n is more than one, X may be represented by like Or unlike alkylene groups.
  • the Rand Rf radicals may be like or unlike and have from 1 to 18 or more carbon atoms in-eachradical.
  • the alkylene group X is a group having at least two carbon atoms and is preferably straight chained. Examples of X wherein the nomenclature of alkylene glycols is adopted, in which a Cal-I4 radical with. two terminal bonds is considered to be. an ethylenegroup follow with the numbers indicating substitution pointsz.
  • X may bepresented :by unlike alkylene groups.
  • Compounds having unlike X groups for example, follow:
  • the blending agents alsoinclude alkylated polyalkylene oxides such as diethyl'poly 1,2- propylene oxide and diisopropyl polyethylene oxide, etc.
  • ACN cetane number improvement over the base fuel.
  • the cetane-improving additive used in Table I 5 is the material disclosed in Patent No. 2,521,698 to Denison et al., and described above.
  • the numbers reported in the following tables are calculated from the cetane numbers obtained by the average of at least three different tests on the same fuel.
  • cetane number can only be obtained up to 100, cetane numbersin excess of this are expressed in terms of cetane (n-hexadecane) plus the number of cubic centimeters of amyl nitrate per gallon of fuel required to match the fuel being tested.
  • Cetane number above 100 is merely a relative term, and determinations of such numbers generally do not have a particularly significant meaning, and therefore, no report has been included of a fuel having a cetane number above 100.
  • a fuel having a cetane number above 100 is compounded by merely increasing the amount of blending agent. For example, it is apparent from Table I that a base fuel containing per cent diethylene glycol diethyl ether and 10 per cent of the cetane-improving additive would result in a fuel having a cetane number substantially above 100.
  • Table II is a tabulation of results obtained when amyl nitrate was used as the cetaneimproving additive and when dimethoxy tetraglycol was used as the blending agent.
  • Table II augment the results obtained in Table I andfurther show the synergistic improvement of different additives plus different blending agents.
  • An outstanding example of the improvement obtained by our invention is the above-compounded diesel fuel oil containing one per cent amyl nitrate, 20 per cent dimethoxytetraglycol, wherein the difference between the calculated improvement and the improvement obtained by actual test engine results was greater than 20 cetane numbers.
  • the amount of cetane-improving additive in diesel fuel oil compositions of our invention varies greately and is generally preferred to be within the range of 0.01 to 10 per cent by weight.
  • the blending agent, allryl ethers, of our invention are usually employed in concentrations greater than 10 per cent by weight.
  • the amount of aliphatic polyethers may vary from about five per cent to about per cent of the total volume of the fuel of this invention with both the fuel-oil base and the polyethers being present in amounts exceeding five per cent by volume.
  • fuels suitable for commercial usage contain less than about 50 per cent by volume of the polyethers.
  • Fuels containing greater amounts of the polyethers are suitable for high-cetane number test fuels.
  • These alkyl ethers may be dior polyethers and have straight chain radicals or branched chain radicals, with the former generally being preferred, although either, or mixtures thereof, may be employed in compositions of our invention.
  • the fuel compositions may be used as cold-engine starting fuels for diesel engines.
  • the fuel-oil base of the compounded diesel fuel oil of our invention may be straight-run or cracked petroleum distillates or derived from synthetic processes or be mixtures thereof and boil in the range of from about 325 F. to about 750 F.
  • the compounded diesel fuel-oil composition is suitable as a fuel for engines of the diesel type, turbine type, and jet type.
  • a compounded fuel comprising at least per cent of a diesel fuel oil, at least 10 per cent by weight of normally liquid oil-soluble blending agents having molecular weights below about 700 and having a formula:
  • R and R are alkyl groups
  • X is a hydrocarbon group of the alkylene type having at least two carbon atoms
  • 12 is an integer
  • n is more than one
  • X is like alkylene groups, and a minor proportion of the order of 0.01 to 10 per cent by weight of a non-benzenoid hydrocarbon peroxide octane-improvement additive.
  • composition of claim 1 wherein the normally liquid oil-soluble compound is dimethoxy tetraglycol.
  • composition of claim 1 wherein the normally liquid oil-soluble compound is diethylene glycol dibutyl ether.
  • composition of claim 1 wherein the normally liquid oil-soluble compound is diethylene glycol diethyl ether.
  • composition of claim 1 wherein said octane-improving additive is a non-benzenoid peroxide material prepared by subjecting a petroleum distillate having a boiling range between 200 and 450 F. and relatively free from asphaltic and resinous materials and from large proportions of aromatic ring compounds to a liquid-phase oxidation treatment with an oxygen containing gas at a temperature within the range of 200 to 400 F. for a period of time suflicient to produce an oil having an oxygen factor higher than 250; contacting the resulting oxygenated oil with 0.1 to 0.75 pounds of 50-90 per cent H2804 per gallon of oil at a temperature of 50 to 85 F.
  • a non-benzenoid peroxide material prepared by subjecting a petroleum distillate having a boiling range between 200 and 450 F. and relatively free from asphaltic and resinous materials and from large proportions of aromatic ring compounds to a liquid-phase oxidation treatment with an oxygen containing gas at a temperature within the range of 200 to 400 F. for a period of time suflic
  • a compounded diesel fuel oil comprising a major proportion of a mixture of a straight-run 8 California crude distillate boiling in the range of about 340 F. to about 700 F. and normally liquid oil-soluble blending agents having molecular weights below about 700 and having the following general formula:
  • R and R. are alkyl groups
  • X is a hydrocarbon group of the alkylene type having at least two carbon atoms
  • n is an integer
  • X is represented by unlike alkylene groups, both components being present in amounts exceeding 5 per cent of the total volume of the fuel oil, and a minor proportion of at least 0.01 per cent but not exceeding 10 per cent by volume of a non-benzenoid hydrocarbon peroxide cetane-improving additive.
  • An improved compression-ignition engine fuel consisting essentially of at least 10 per cent of a diesel fuel oil, at least 10 per cent by weight of diethylene glycol diethyl ether as a blending agent, and a minor proportion of a non-benzenoid hydrocarbon peroxide as a octane-improvement additive.
  • An improved compression-ignition engine fuel comprising a major proportion of a mixture of a fuel-oil base boiling in the range of about 325 F. to about 750 F. and an oil-soluble aliphatic polyether blending agent having a molecular weight below about 700 and the general formula:
  • R, and R are alkyl groups
  • X is a hydrocarbon group of the alkylene type having at least two carbon atoms and n is an integer, both components of the mixture being present in amounts exceeding 5% of the total volume of the fuel, and a minor proportion not exceeding 10% of the total volume of the fuel of a non-benzenoid hydrocarbon peroxide.
  • An improved compression-ignition engine fuel comprising a fuel-oil base boiling in the range of about 325 F. to about 750 F. containing an oilsoluble aliphatic polyether blending agent weight below about 700 and the general formula:
  • R and R are alkyl groups
  • X is a hydrocarbon group of the alkylene type having at least two carbon atoms and n is an integer, in amounts exceeding 5% of the total volume of the fuel, and
  • a octane-improving agent present in amounts not exceeding 10% of the total volume of the fuel, said octane-improving agent comprising a mixture of amyl nitrate and a peroxide wherein said peroxide is a material prepared by subjecting a petroleum distillate having a boiling range between 200 and 450 and relatively free from asphaltic and resinous materials and from large proportions of aromatic ring components to a liquid-phase oxidation treatment with an oxygencontaining gas at a temperature within the range of 200 to 400 F. for a period of time sufficient 9 between 60 and 95% of said oxygenated oil to obtain a concentrate or relatively stable cetane-improving oxygenated oil.
  • An improved compression-ignition engine fuel comprising a major proportion of a mixture of a i'uel-oil base boiling in the range of about 325 F. to about 750 F. and an oil-soluble aliphatic polyether blending agent having a mole ular weight below about 700 and the general formula:
  • R and R alkyl groups wherein R and R alkyl groups, X is a hydrocarbon group of the alkylene type having at least two carbon atoms and n is an integer, both com 1%) ponents of the mixture being present in amounts exceeding 5% of the total volume of the fuel, and a minor proportion not exceeding 10% of the total volume of the fuel of alkyl peroxides.

Description

Patented Oct. 13, 195 3 DIESEL FUEL OIL Maurice R. Barusch, Richmond, and Robert Y.
Mixer, Los Angeles, Calif., assignors to California Research Corporation, San Francisco,
Calif., a corporation of Delaware No Drawing. Application May 24, 1949, Serial No. 95,146
10 Claims.
This invention relates to an improved diesel fuel oil, and more particularly to improved diesel fuel-oil compositions having high cetane numbers.
Diesel engines depend upon the heat developed by compressing a charge of air to ignite the fuel injected into the engine cylinder after the air is compressed. A high compression ratio is necessary because most known diesel fuels require a relatively high compression ratio in order to ignite. A factor of major importance in regard to the performance of a diesel fuel oil is the delay in ignition from the beginning of the injection of the fuel to the beginning of its combustion. This property is commonly termed the ignitiondelay characteristic of the fuel and may be expressed in terms of cetane numbers. If ignition delay is too long, the motor fuel will accumulate in the cylinder until it reaches ignition conditions and then will burn rapidly, causing a sudden pressure increase which may result in engine knocking. In addition, too long an ignition delay may result in a smoky exhaust, a decrease in en'- gine efliciency, and possibly crankcase-oil dilution.
One of the more important difficulties that arises through the use of diesel engines is the problem of starting the engine when it is cold. It is quite common, when using many presently known diesel fuels, to employ special starting pro- I cedures wherein various starting fuels, such as ether, are employed. During the warm-up period of the diesel engines, considerable uneven ignition of the fuel may occur in the engine.
An object of the present invention is to provide a diesel fuel-oil composition having a high cetane number that ignites readily and functions smoothly under operating conditions.
Another object of this invention is to provide a diesel fuel-oil composition that is readily adaptable for starting cold diesel engines.
Still another object of this invention is to provide a high octane number diesel fuel-oil composition whose base has a low cetane number.
A further object of this invention is to provide a diesel fuel-oil composition that may be used as a reference fuel for fuels having cetane numbers in excess of 100.
In order to meet the increasing demand for diesel fuel oils having high octane numbers, various octane-improving materials have been added to the petroleum fuel oil base. The use of cetaneimproving materials has also permitted the employment of base fuels having relatively low cetane numbers and has thereby increased, in many instances, the usefulness of middle-ofthe-barrel stock to the refiners. The cetaneimproving materials have been generally of an additive or blend type. The characteristics and properties of these are described below.
2 We have discovered that when normally liquid oil-soluble aliphatic polyethers, especially those having molecular weights below about 700 with a general formula:
produces a relatively large cetane improvement when added in a small concentration to a diesel fuel oil. The improvement is independent of the cetane numberof the additive and does not produce a corresponding cetane improvement when added in additional incremental amounts. Generally the amount of a octane-improving additive added to a diesel fuel oil is in the range of about .001 per cent to about 10 per cent.
Suitable additives which may be employed as the cetane-improving additive are: alkyl nitrate and nitrites; nitroso compounds; di-azo compounds; di-sulfides; and hydrocarbon peroxides such as di-alkyl peroxides and alkyl hydroperoxides, including peroxides of the tertiary type and corresponding alicyclic peroxides, and acyl peroxides. The alkyl peroxides and hydroperoxides include the following specific compounds: ethyl peroxide and hydroperoxide; isobutene peroxides and hydroperoxides; isopentene peroxides and hydroperoxides; 2-methylpentane peroxides and hydroperoxides; 2-ethyl butene peroxide and hydroperoxide; 2-methylpentane peroxides and hydroperoxides; 3-methylpentane peroxide and hydroperoxide; 2,3-dimethyl butane peroxide and hydroperoxide; and 2,4-dimethylbutane peroxide and hydroperoxide. Peroxides of the di(tertiary alkyl) type include: di(tertiary butyl) peroxide; di (tertiary amyl) peroxide; di (21-"nethyl, 2-pentyl) peroxide; di(3-methyl,3-pentyl) peroxide; di(2-ethyl,2-butyl) peroxide; di(l-halo, 2-propyl) peroxide; di(1-halo,2-methyl,2-butyl) peroxide; di(1-halo,3-methyl,3-butyl) peroxide; di(Z halo, 3 -methyl,3 butyl) peroxide; di(lphenyl,1-methyl,1-propyl) peroxide, and di(lphenyl,2-methyl,2-propyl) peroxide. Cyclic hydrocarbon peroxides include; cyclopentyl hydroperoxide; methylcyclopentyl hydroperoxides; the isomeric dimethylcyclopentyl hydroperoxides; ethylcyclopentyl peroxides; the isomeric diethylcyclopentyl hydroperoxides; the isomeric methylethylcyclopentyl hydroperoxides, cyclohexyl hydroperoxide, methylcyclohexyl hydroperoxides; the isomeric dimethylcyclohexyl hydroperoxides; ethylcyclohexyl hydroperoxides; the isomeric diethylcyclohexyl hydroperoxides; l-4-methyl isopropylcyclohexyl hydroperoxide; hydroperoxides of cyclopentane, cycloheptane, etc., andhigher molecular weight substituted cycloparafiins. Asymmetrical dialkyl peroxides may also be used.
Peroxides especially suitable for the composition of our invention are non-benzenoid hydrocarbon peroxides which; include the aliphatic and alicyclic peroxides. non-benzenoid peroxides is illustrated by the cetane-improving additive disclosed in Schultz et al. Patent No. 2,317,968 and is prepared by partially oxidizing a petroleum distillate rela-v tively free from asphaltic and resinous materials,
and from large proportions of aromatic ring compounds, and of a higher volatility than kerosene with an oxygen-containing gas under liquid-phase conditions at a temperature of 275 to 310 F. for a suflicient length of time toproduce an oil having an oxygenfactor (obtained by dissolving an oil samplein 70 cc. of chloroform and 25 cc. of acetic acid and then adding 2 cc. of saturatedKI to the solution, agitating for 3 minutes, followed by titrating liberated iodine with NazSzOs and calculating the results according to the equation: titer in ml. normality of the thiosulphatex1120/volume of sample in ml.) higher than. 800, but insufficient to increase the neutralization number of the oil by more than 20, then arresting said treatment before the oxygen factor of the produced oil decreases to below 800 and then removing. the acidic reaction products from the produced oil without reducing the oxygen factor to below about 800.
Patent to Denison et al., No. 2,521,698, discloses another especially desirable non-benzenoid hydrocarbon peroxide for. the composition of our invention which may be used as a cetane-improving material and that is prepared by subjecting a petroleum distillate having a boiling range between 200 and 450 and relatively free from asphaltic and resinous materials and from large proportions of aromatic ring compounds to a liquid-phase oxidation treatment with an oxygen-containing gas at a temperature within the range of 200 to 400 F. for a period of time, suiiicient to produce an oil having an oxygen factor higher than 250; contacting the resulting oxygenated oil with 0.1 to 0.75 pound of 50-90 per cent H2804 per gallon of oil at a temperature of 50 to 85 F. for less than 90 minutes, thereby producin a more stable and less corrosion-producing oil having a substantially-lowered oxygen factor, treating this oil with controlled amounts of weak caustic solution to remove acidic material, and, concentrating the caustic-treated oil by fractional distillation to a temperature below 350 F. and a pressure be-' tween 10 mm. of mercury and atmospheric to volatilize between 60 and 95 per cent-ofsaid oxygenated oil to obtain a concentrate of relatively stable octane-improving oxygenated oil.
The term blending agent as used herein and in the appended claims is a material which produces a cetane improvement in diesel fuel oils corresponding to the amount of blending agent added and the cetane number of the blending agent. The amount of blending agent generally added to diesel fueloils is above about 5 per cent.
The aliphatic polyether blendin agents especially suitable for the composition of this invention are normally liquid oil-soluble aliphatic polyethers especially alkyl polyethers having a An example of these molecular weight .belowabout '700;'with; a;general formula:
R(OX) n-OR wherein R and R are like or unlike alkyl groups, X' islahydrocarbon group of the alkylene type having at least two carbon atoms, nis an integer, and when n is more than one, X may be represented by like Or unlike alkylene groups. The Rand Rf radicals may be like or unlike and have from 1 to 18 or more carbon atoms in-eachradical. The alkylene group X is a group having at least two carbon atoms and is preferably straight chained. Examples of X wherein the nomenclature of alkylene glycols is adopted, in which a Cal-I4 radical with. two terminal bonds is considered to be. an ethylenegroup follow with the numbers indicating substitution pointsz. ethylene; 1,2 propylene; 1,3 propylene; L2: butylene; 1,3,buty1ene; 1,4 butylene; 2,3 butylene; 1,2 pentylene; 1,3 pentylene; 1,4 pentylene; 1,5 pentylene; 2,3 pentylene; 2,4 pentylene; 1,2, hexylene; 1,3.hexylene; 1,4 hexylene; 1,5 jhe x'y -l ene; 1,6 hexylene; 2,3 hexylene; 2,4 hexylene; 2,5- hexylene, 3,4 hexylene; 1,2 heptylene; 1,3
heptylene; 1,4 heptylene; 1,5, heptylene; 1,6; heptylene; 1,7 heptylene; 2,3 heptylene; 2%;4' heptylene; 2,5 heptylene; 2,6 heptylene;- 3,-4
heptylene; 3,5 heptylene; 1,2floctylene; 1,3octylene; 1,4 octylene; 1,5 octylene; 1,6 octylene; 1,f7 octylene; 1,8 octylene; 2,3.octylene; 2,4 octylene; 2,5.octylene; 2,6 octylene; 2,7 octylene; 3,4 octylene; 3,5 octylene; 4,5 octylene; 3 ethy1,-2'-4 hexylene; 1,3 dimethyl-2 ethyl-1,4 butylene, etc.-
As explained above, X may bepresented :by unlike alkylene groups. Compounds having unlike X groups, for example, follow:
The blending agents alsoinclude alkylated polyalkylene oxides such as diethyl'poly 1,2- propylene oxide and diisopropyl polyethylene oxide, etc.
The following examples illustrate cetaneimprovement obtained with compositions of this invention.
The base fuel used in the examples below had the following inspection:
Source Straight-run California crude. A P I 37 6 Viscosity at F 1.052 centistokes;
of fuels given in the tables below was A. S. T. M. Test No. D613-47T.
The symbol ACN is used below to. denote cetane number improvement over the base fuel.
The cetane-improving additive used in Table I 5 is the material disclosed in Patent No. 2,521,698 to Denison et al., and described above. The numbers reported in the following tables are calculated from the cetane numbers obtained by the average of at least three different tests on the same fuel.
TABLE I ACN pro- AON proiifi t t. t t? i" I 1e y y e 1e y $335353 gr- ,gggg gg g stills gggg G0 1- ,1 V- ing additive ethyl mg addi ethyl culated ether tive ether (alone) (alone) 1 7 s 17 1 20 1 15 22 27 1 3o 7 32 3s 2 1o 10 8 18 22 2 20 1o 15 25 so 2 so 10 25 35 42 10 10 23 s 31 a5 10 20 2a 15 as 46 10 so 23 25 4s 57 From the foregoing table, it is apparent that the ACN observed in all cases was substantially above the expected improvement which would be the summation of the cetane improvement obtained separately from the cetane-improving additive and from the diethylene glycol diethyl ether. Since cetane number can only be obtained up to 100, cetane numbersin excess of this are expressed in terms of cetane (n-hexadecane) plus the number of cubic centimeters of amyl nitrate per gallon of fuel required to match the fuel being tested. Cetane number above 100 is merely a relative term, and determinations of such numbers generally do not have a particularly significant meaning, and therefore, no report has been included of a fuel having a cetane number above 100. However, as can be seen from the above table, a fuel having a cetane number above 100 is compounded by merely increasing the amount of blending agent. For example, it is apparent from Table I that a base fuel containing per cent diethylene glycol diethyl ether and 10 per cent of the cetane-improving additive would result in a fuel having a cetane number substantially above 100.
Table II, below, is a tabulation of results obtained when amyl nitrate was used as the cetaneimproving additive and when dimethoxy tetraglycol was used as the blending agent.
The results of Table II augment the results obtained in Table I andfurther show the synergistic improvement of different additives plus different blending agents. An outstanding example of the improvement obtained by our invention is the above-compounded diesel fuel oil containing one per cent amyl nitrate, 20 per cent dimethoxytetraglycol, wherein the difference between the calculated improvement and the improvement obtained by actual test engine results was greater than 20 cetane numbers.
A further test was made to indicate the improvement obtainable with a composition of our invention. In this test, a diesel fuel oil of the base given above, was compounded with one per cent each of the cetane-improving additives 01' Table I and II and additionally contained 20 per cent of dimethoxy tetraglycol. The calculated cetane improvement was 37, but the measured improvement from actual test engine results showed an improvement of 50. Thus again this shows the cetane improvement obtainable with compositions cf our invention.
To further illustrate the advantage obtainable by employing a diesel fuel oil composition of our invention, an addition of 10 per cent dimethoxy tetraglycol was made to the base fuel and caused an increase of 7 cetane numbers. To another sample of the base fuel was added 0.5 per cent amyl nitrate and this addition caused an increase of 9 numbers. A one-to-one mixture of these two blends produced a fuel which had a 12 number increase above the base stock which is considerably above the expected number improvement. Normally when two fuels of different cetane number are blended in equal proportion, the resulting fuel has a cetane number equal to the average of its components.
In another example, equal portions of a fuel containing 10 per cent of the cetane-improving additive of Table I, which increased the rating of the base fuel 23 numbers, and a fuel containing 35 per cent ethylene glycol dibutyl ether, which caused an increased rating of 20 numbers, were blended in a one-to-one ratio. The resultant fuel rated 32 numbers above the base stock and again above the expected or calculated average of 21.5 numbers,
When ethylene glycol dibutyl ether was added in equal proportions to a petroleum distillate having a cetane number of 43, the resulting fuel had a cetane number of 78. Five per cent of tertiary butyl hydroperoxide increased the cetane number of the petroleum distillate from 43 to 83. A oneto-one mixture of these blended fuels resulted in an increase of 45 cetane numbers over the base fuel or 7 cetane numbers above the expected value.
The addition of one per cent ditertiary butyl peroxide gave an increase of 1l cetane numbers to a base fuel having a cetane number of 43. When 15 per cent of diethylene glycol diethyl ether was added to a base fuel having a 43 cetane number, an increase of 12 cetane numbers resulted. However, when a one-to-one blend of these two fuels was made a 1'7 cetane number over the 43 resulted. This is 5.5 numbers above theexpected calculated value.
The amount of cetane-improving additive in diesel fuel oil compositions of our invention varies greately and is generally preferred to be within the range of 0.01 to 10 per cent by weight. The blending agent, allryl ethers, of our invention are usually employed in concentrations greater than 10 per cent by weight. However, the amount of aliphatic polyethers may vary from about five per cent to about per cent of the total volume of the fuel of this invention with both the fuel-oil base and the polyethers being present in amounts exceeding five per cent by volume. Ordinarily, fuels suitable for commercial usage contain less than about 50 per cent by volume of the polyethers. Fuels containing greater amounts of the polyethers are suitable for high-cetane number test fuels. These alkyl ethers may be dior polyethers and have straight chain radicals or branched chain radicals, with the former generally being preferred, although either, or mixtures thereof, may be employed in compositions of our invention.
Because of the high octane numbers available with compositions of our invention, the fuel compositions may be used as cold-engine starting fuels for diesel engines.
The fuel-oil base of the compounded diesel fuel oil of our invention may be straight-run or cracked petroleum distillates or derived from synthetic processes or be mixtures thereof and boil in the range of from about 325 F. to about 750 F. The compounded diesel fuel-oil composition is suitable as a fuel for engines of the diesel type, turbine type, and jet type.
While various specific embodiments of the in vention have been illustrated and described, many modifications and adaptations may be made without departing from this invention, and all such changes as are intended to be included within the scope of the claims.
We claim:
1. A compounded fuel comprising at least per cent of a diesel fuel oil, at least 10 per cent by weight of normally liquid oil-soluble blending agents having molecular weights below about 700 and having a formula:
wherein R and R are alkyl groups, X is a hydrocarbon group of the alkylene type having at least two carbon atoms, 12 is an integer, and when n is more than one, X is like alkylene groups, and a minor proportion of the order of 0.01 to 10 per cent by weight of a non-benzenoid hydrocarbon peroxide octane-improvement additive.
2. The composition of claim 1, wherein the normally liquid oil-soluble compound is dimethoxy tetraglycol.
3. The composition of claim 1, wherein the normally liquid oil-soluble compound is diethylene glycol dibutyl ether.
41. lhe composition of claim 1, wherein the normally liquid oil-soluble compound is diethylene glycol diethyl ether.
5. The composition of claim 1, wherein said octane-improving additive is a non-benzenoid peroxide material prepared by subjecting a petroleum distillate having a boiling range between 200 and 450 F. and relatively free from asphaltic and resinous materials and from large proportions of aromatic ring compounds to a liquid-phase oxidation treatment with an oxygen containing gas at a temperature within the range of 200 to 400 F. for a period of time suflicient to produce an oil having an oxygen factor higher than 250; contacting the resulting oxygenated oil with 0.1 to 0.75 pounds of 50-90 per cent H2804 per gallon of oil at a temperature of 50 to 85 F. for less than 90 minutes, thereby producing a more stable and less corrosion-producing oil having a substantially lowered oxygen factor, treating this oil with controlled amounts of weak caustic solution to remove acidic material, and concentrating the caustic-treated oil by fractional distillation at a temperature below 350 F. and a pressure between 10 mm. of mercury and atmospheric to volatilize between 60 and 95 per cent of said oxygenated oil to obtain a concentrate of relatively stable cetaneimproving oxygenated oil.
6. A compounded diesel fuel oil comprising a major proportion of a mixture of a straight-run 8 California crude distillate boiling in the range of about 340 F. to about 700 F. and normally liquid oil-soluble blending agents having molecular weights below about 700 and having the following general formula:
R('OX) n-0-R' wherein R and R. are alkyl groups, X is a hydrocarbon group of the alkylene type having at least two carbon atoms, n is an integer, and when n is more than one, X is represented by unlike alkylene groups, both components being present in amounts exceeding 5 per cent of the total volume of the fuel oil, and a minor proportion of at least 0.01 per cent but not exceeding 10 per cent by volume of a non-benzenoid hydrocarbon peroxide cetane-improving additive.
7. An improved compression-ignition engine fuel consisting essentially of at least 10 per cent of a diesel fuel oil, at least 10 per cent by weight of diethylene glycol diethyl ether as a blending agent, and a minor proportion of a non-benzenoid hydrocarbon peroxide as a octane-improvement additive.
8. An improved compression-ignition engine fuel comprising a major proportion of a mixture of a fuel-oil base boiling in the range of about 325 F. to about 750 F. and an oil-soluble aliphatic polyether blending agent having a molecular weight below about 700 and the general formula:
wherein R, and R are alkyl groups, X is a hydrocarbon group of the alkylene type having at least two carbon atoms and n is an integer, both components of the mixture being present in amounts exceeding 5% of the total volume of the fuel, and a minor proportion not exceeding 10% of the total volume of the fuel of a non-benzenoid hydrocarbon peroxide.
9. An improved compression-ignition engine fuel comprising a fuel-oil base boiling in the range of about 325 F. to about 750 F. containing an oilsoluble aliphatic polyether blending agent weight below about 700 and the general formula:
wherein R and R are alkyl groups, X is a hydrocarbon group of the alkylene type having at least two carbon atoms and n is an integer, in amounts exceeding 5% of the total volume of the fuel, and
a octane-improving agent present in amounts not exceeding 10% of the total volume of the fuel, said octane-improving agent comprising a mixture of amyl nitrate and a peroxide wherein said peroxide is a material prepared by subjecting a petroleum distillate having a boiling range between 200 and 450 and relatively free from asphaltic and resinous materials and from large proportions of aromatic ring components to a liquid-phase oxidation treatment with an oxygencontaining gas at a temperature within the range of 200 to 400 F. for a period of time sufficient 9 between 60 and 95% of said oxygenated oil to obtain a concentrate or relatively stable cetane-improving oxygenated oil.
10. An improved compression-ignition engine fuel comprising a major proportion of a mixture of a i'uel-oil base boiling in the range of about 325 F. to about 750 F. and an oil-soluble aliphatic polyether blending agent having a mole ular weight below about 700 and the general formula:
wherein R and R alkyl groups, X is a hydrocarbon group of the alkylene type having at least two carbon atoms and n is an integer, both com 1%) ponents of the mixture being present in amounts exceeding 5% of the total volume of the fuel, and a minor proportion not exceeding 10% of the total volume of the fuel of alkyl peroxides.
MAURICE R. BARUSCH. ROBERT Y. MIXER.
References Cited in the file of this patent

Claims (1)

1. A COMPOUNDED FUEL COMPRISING AT LEAST 10 PER CENT OF A DIESEL FUEL OIL, AT LEST 10 PER CENT BY WEIGHT OF NORMALLY LIQUID OIL-SOLUBLE BLENDING AGENTS HAVING MOLECULAR WEIGHTS BELOW ABOUT 700 AND HAVING A FORMULA
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Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2763537A (en) * 1949-05-24 1956-09-18 California Research Corp Diesel fuel oil
US2785662A (en) * 1953-04-06 1957-03-19 Leonard D Boyce Compositions and methods for removing deposits
US2842432A (en) * 1953-12-07 1958-07-08 Texas Co Supplementary fuel mixture for cold starting diesel engines
US2877102A (en) * 1955-11-09 1959-03-10 Rohm & Haas Diesel oil improvers
US2891851A (en) * 1956-07-20 1959-06-23 Shell Dev Fuel for internal combustion engines
US2912313A (en) * 1956-03-30 1959-11-10 Ethyl Corp Diesel fuel
US2934048A (en) * 1955-10-13 1960-04-26 Sinclair Refining Co Composition
US2971828A (en) * 1961-02-14 Hydrazese-containing fuel oil
DE1102477B (en) * 1955-11-11 1961-03-16 Iashellia Res Ltd Liquid petrol-based fuel for gasoline engines
US3108864A (en) * 1960-07-13 1963-10-29 California Research Corp Engine starting fluid
EP0255115A1 (en) * 1986-07-31 1988-02-03 Wynn Oil Company Gasoline additive composition
US4740215A (en) * 1987-01-27 1988-04-26 Union Oil Company Of California Composition for cetane improvement of diesel fuels
US5024678A (en) * 1987-04-09 1991-06-18 Dea Mineralol Aktiengesellschaft Process for the prevention or reduction of deposits in carburetors, injection devices and similar devices of engines
US5308365A (en) * 1993-08-31 1994-05-03 Arco Chemical Technology, L.P. Diesel fuel
US5314511A (en) * 1992-12-23 1994-05-24 Arco Chemical Technology, L.P. Diesel fuel
US5405417A (en) * 1990-07-16 1995-04-11 Ethyl Corporation Fuel compositions with enhanced combustion characteristics
US5425790A (en) * 1992-12-23 1995-06-20 Arco Chemical Technology, L.P. Diesel fuel
DE19843380A1 (en) * 1998-09-22 2000-03-23 Kief Horst Process for reducing the pollutant emissions from I.C. engines comprises adding glyoxal in an aqueous solution to the fuel
EP1070755A1 (en) * 1999-07-22 2001-01-24 SNAMPROGETTI S.p.A. Liquid mixture consisting of diesel gas oils and oxygenated compounds
WO2005010131A1 (en) 2003-06-24 2005-02-03 Michiel Arjaan Kousemaker Method for producing an oxygen-containing compound used as fuel additive, in particular in diesel fuels, gasoline and rapeseed methyl ester
WO2018055065A1 (en) 2016-09-21 2018-03-29 Cepsa S.A.U. Solketal-ethers, production method and uses thereof

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US2221839A (en) * 1936-10-20 1940-11-19 Atlantic Refining Co Fuel for compression ignition engines
US2317968A (en) * 1941-05-12 1943-04-27 Standard Oil Co California Compression ignition motor fuel
US2521698A (en) * 1946-05-02 1950-09-12 California Research Corp Injection engine fuel

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US2221839A (en) * 1936-10-20 1940-11-19 Atlantic Refining Co Fuel for compression ignition engines
US2317968A (en) * 1941-05-12 1943-04-27 Standard Oil Co California Compression ignition motor fuel
US2521698A (en) * 1946-05-02 1950-09-12 California Research Corp Injection engine fuel

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2971828A (en) * 1961-02-14 Hydrazese-containing fuel oil
US2763537A (en) * 1949-05-24 1956-09-18 California Research Corp Diesel fuel oil
US2785662A (en) * 1953-04-06 1957-03-19 Leonard D Boyce Compositions and methods for removing deposits
US2842432A (en) * 1953-12-07 1958-07-08 Texas Co Supplementary fuel mixture for cold starting diesel engines
US2934048A (en) * 1955-10-13 1960-04-26 Sinclair Refining Co Composition
US2877102A (en) * 1955-11-09 1959-03-10 Rohm & Haas Diesel oil improvers
DE1102477B (en) * 1955-11-11 1961-03-16 Iashellia Res Ltd Liquid petrol-based fuel for gasoline engines
US2912313A (en) * 1956-03-30 1959-11-10 Ethyl Corp Diesel fuel
US2891851A (en) * 1956-07-20 1959-06-23 Shell Dev Fuel for internal combustion engines
US3108864A (en) * 1960-07-13 1963-10-29 California Research Corp Engine starting fluid
EP0255115A1 (en) * 1986-07-31 1988-02-03 Wynn Oil Company Gasoline additive composition
US4740215A (en) * 1987-01-27 1988-04-26 Union Oil Company Of California Composition for cetane improvement of diesel fuels
US5024678A (en) * 1987-04-09 1991-06-18 Dea Mineralol Aktiengesellschaft Process for the prevention or reduction of deposits in carburetors, injection devices and similar devices of engines
US5405417A (en) * 1990-07-16 1995-04-11 Ethyl Corporation Fuel compositions with enhanced combustion characteristics
US5314511A (en) * 1992-12-23 1994-05-24 Arco Chemical Technology, L.P. Diesel fuel
US5425790A (en) * 1992-12-23 1995-06-20 Arco Chemical Technology, L.P. Diesel fuel
US5308365A (en) * 1993-08-31 1994-05-03 Arco Chemical Technology, L.P. Diesel fuel
DE19843380A1 (en) * 1998-09-22 2000-03-23 Kief Horst Process for reducing the pollutant emissions from I.C. engines comprises adding glyoxal in an aqueous solution to the fuel
EP1070755A1 (en) * 1999-07-22 2001-01-24 SNAMPROGETTI S.p.A. Liquid mixture consisting of diesel gas oils and oxygenated compounds
US20030159341A1 (en) * 1999-07-22 2003-08-28 Snamprogetti S.P.A. Liquid mixture consisting of diesel gas oils and oxygenated compounds
WO2005010131A1 (en) 2003-06-24 2005-02-03 Michiel Arjaan Kousemaker Method for producing an oxygen-containing compound used as fuel additive, in particular in diesel fuels, gasoline and rapeseed methyl ester
US20090270643A1 (en) * 2003-06-24 2009-10-29 Michiel Arjaan Kousemaker Method for producing an oxygen-containing compound used as fuel additive, in particular in diesel fuels, gasoline, and rapeseed methyl ester
EP2204434A1 (en) 2003-06-24 2010-07-07 Biovalue Holding BV Process for making an oxygenate as an additive in fuels, particularly in diesel fuels, gasoline and rapeseed methyl ester
WO2018055065A1 (en) 2016-09-21 2018-03-29 Cepsa S.A.U. Solketal-ethers, production method and uses thereof

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