US20080134571A1 - Unleaded fuel compositions - Google Patents

Unleaded fuel compositions Download PDF

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Publication number
US20080134571A1
US20080134571A1 US11/609,742 US60974206A US2008134571A1 US 20080134571 A1 US20080134571 A1 US 20080134571A1 US 60974206 A US60974206 A US 60974206A US 2008134571 A1 US2008134571 A1 US 2008134571A1
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vol
fuel composition
unleaded fuel
unleaded
group
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US11/609,742
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Jorg Landschof
Michael Clifford MACKNAY
Timothy Michael SHEA
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Shell USA Inc
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Priority to US11/609,742 priority Critical patent/US20080134571A1/en
Assigned to SHELL OIL COMPANY reassignment SHELL OIL COMPANY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: LANDSCHOF, JORG, MACKNAY, MICHAEL CLIFFORD, SHEA, TIMOTHY MICHAEL
Publication of US20080134571A1 publication Critical patent/US20080134571A1/en
Priority to US13/324,166 priority patent/US20120080000A1/en
Priority to US13/553,505 priority patent/US9074153B2/en
Abandoned legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/04Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • C10L1/06Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark ignition
    • 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
    • C10L1/02Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • C10L1/023Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only for spark ignition
    • 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
    • C10L1/222Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
    • C10L1/223Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond having at least one amino group bound to an aromatic carbon atom
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/10Use of additives to fuels or fires for particular purposes for improving the octane number

Definitions

  • the present application relates to unleaded fuel compositions.
  • the octane rating of the fuel must be high enough to prevent knocking.
  • Gasolines sold at service stations typically have an octane rating of from about 87 to about 93. Fuels having such octane ratings are satisfactory for most automotive engines.
  • the present application provides unleaded fuel compositions having an octane rating of 105 or more.
  • the present application provides unleaded fuel compositions having an octane rating greater than 105.
  • the present application provides unleaded fuel compositions having an octane rating of 106 or more.
  • the present application also provides unleaded fuel compositions having an octane rating of 110 or more.
  • the present application also provides an unleaded fuel composition
  • an unleaded fuel composition comprising: a combination of alkylated benzenes comprising alkyl groups having from 1 to 4 carbon atoms; 5 vol. % or more of one or more aromatic amines; and, an isoparaffin composition selected from the group consisting of alkylate, a combination of isoparaffins having a total number of carbon atoms of 11 or less, and combinations thereof.
  • the present application also provides an unleaded fuel composition comprising: an isoparaffin composition comprising alkylate; a combination of alkylated benzenes comprising alkyl groups having from 1 to 4 carbon atoms; and, one or more aromatic amines comprising an aromatic ring comprising an amine substituent.
  • the present application also provides an unleaded fuel composition comprising: from about 40 vol. % to about 50 vol. % alkylate; from about 30 vol. % to about 40 vol. % toluene; from about 10 vol. % to about 20 vol. % m-xylene; and, from 2 vol. % to about 12 vol. % aniline.
  • the present application also provides an unleaded fuel composition
  • an unleaded fuel composition comprising: about 44 vol. % alkylate comprising about 70 vol. % or more isoparaffins having a total of 8 carbon atoms; about 34 vol. % toluene; about 15 vol. % m-xylene; and, about 7 vol. % aniline.
  • the present application provides unleaded fuel compositions having an octane rating which is higher than typically demonstrated by similar unleaded fuels.
  • the unleaded fuels of the present application comprise aromatic amine, which is believed to contribute to a higher octane rating.
  • the unleaded fuel compositions it is advantageous for the unleaded fuel compositions to have an octane rating sufficiently high to prevent knocking. In high performance applications, it is advantageous for unleaded fuel compositions to have an octane rating sufficiently high to boost power output from the high performance engine. In one embodiment, the application provides an unleaded racing fuel having an octane rating sufficiently high to boost the power output from a racing engine.
  • the octane rating of a fuel composition generally is calculated as the sum of the Research Octane Number (RON) and the Motor Octane Number (MON) divided by 2, i.e., (R+M)/2. Unless otherwise indicated, the Research Octane Number (RON) is determined according to method ASTM D-2699-04a (2004) and the Motor Octane Number (MON) is determined according to method ASTM D-2700-04a (2004), both incorporated by reference.
  • the unleaded fuel composition of the present application has an octane rating of about 105 or more. In one embodiment, the unleaded fuel composition has an octane rating of greater than 105. In another embodiment, the unleaded fuel composition of the present application has an octane rating of about 106 or more. In one embodiment, the unleaded fuel composition has an octane rating of about 110 or more.
  • the unleaded fuel composition comprises: a combination of alkylated benzenes; one or more aromatic amines; and, an isoparaffin composition selected from the group consisting of alkylate, a combination of isoparaffins having a total number of carbon atoms of 11 or less, and combinations thereof.
  • the unleaded fuel composition comprises: an isoparaffin composition comprising alkylate; a combination of alkylated benzenes; and, one or more aromatic amine.
  • This embodiment has the advantage of being relatively less costly due to the use of isoparaffin composition comprising alkylate.
  • the unleaded fuel composition optionally comprises one or more oxygenate octane booster.
  • the unleaded fuel composition also optionally comprises one or more additional additives.
  • the unleaded fuel composition comprises a combination of alkylated benzenes.
  • the unleaded fuel composition comprises about 20 vol. % or more of a combination of alkylated benzenes.
  • vol. % is based on the total volume of the unleaded fuel composition, unless otherwise indicated.
  • the unleaded fuel composition comprises about 25 vol. % or more alkylated benzenes.
  • the unleaded fuel composition comprises about 40 vol. % or more alkylated benzenes.
  • the unleaded fuel composition comprises about 60 vol. % or less alkylated benzenes. In one embodiment, the unleaded fuel composition comprises about 55 vol. % or less alkylated benzenes. In yet another embodiment, the unleaded fuel composition comprises about 50 vol. % or less alkylated benzenes.
  • Suitable alkylated benzenes have the following general structure:
  • R, R 1 , and R 2 are selected from the group consisting of hydrogen and alkyl groups having from 1 to 4 carbon atoms, provided that at least one of R, R 1 , and R 2 is an alkyl group.
  • R, R 1 , and R are selected from the group consisting of hydrogen and alkyl groups having from 1 to 2 carbon atoms.
  • R, R 1 , and R 2 are selected from the group consisting of hydrogen and methyl groups.
  • the alkylated benzene is mono-alkylated benzene.
  • the alkylated benzene is a di-alkylated benzene.
  • the alkylated benzene is a tri-alkylated benzene.
  • one or more of R, R 1 , and R are methyl groups.
  • the alkylated benzenes are a combination of mono-alkylated benzene, di-alkylated benzene, and tri-alkylated benzene.
  • the unleaded fuel composition comprises a combination of monomethyl benzene and dimethyl benzene. In one embodiment, the combination further comprises trimethyl benzene. In one embodiment, the unleaded fuel composition comprises a combination of xylene and toluene. In one embodiment, the unleaded fuel composition further comprises 1,3,5-trimethylbenzene.
  • the unleaded fuel composition also comprises one or more aromatic amine.
  • the unleaded fuel composition For lower performance applications, it is possible for the unleaded fuel composition to comprise about 0.1 vol. % or more of one or more aromatic amine. This is particularly true where the isoparaffin comprises the less expensive alkylate. In one embodiment, the unleaded fuel composition comprises about 0.5 vol. % or more of the aromatic amine. In one embodiment, the unleaded fuel composition comprises about 1 vol. % or more of the aromatic amine. In one embodiment, the unleaded fuel composition comprises about 2 vol. % or more of the aromatic amine.
  • the unleaded fuel composition comprises 5 vol. % or more of the aromatic amine. In one embodiment, the unleaded fuel composition comprises greater 5 vol. % of the aromatic amine. In one embodiment, the unleaded fuel composition comprises about 6 vol. % or more of the aromatic amine. In another embodiment, the unleaded fuel composition comprises about 7 vol. % or more of the aromatic amine.
  • the unleaded fuel composition comprises about 15 vol. % or less of the aromatic amine. In one embodiment, the unleaded fuel composition comprises from about 10 vol. % or less of the aromatic amine. In one embodiment, the unleaded fuel composition comprises 8 vol. % or less of the aromatic amine. In one embodiment, the unleaded fuel composition contains about 7 vol. % of the aromatic amine.
  • aromatic amine refers to one or more aromatic amines having the following general structure:
  • R 3 , R 4 and R 5 independently are selected from the group consisting of hydrogen and alkyl groups having from about 1 to 4 carbon atoms.
  • R 3 is hydrogen.
  • the alkyl groups have from about 1 to 2 carbon atoms.
  • the alkyl groups are methyl groups.
  • R 3 , R 4 and R 5 are hydrogens.
  • the aromatic amine has one or more alkyl substituents on the aromatic ring.
  • the alkyl group may be at any position relative to the nitrogen containing substituent.
  • the alkyl group is at a meta-position relative to the nitrogen containing substituent.
  • the alkyl group is at a para-position relative to the nitrogen containing substituent.
  • the nitrogen bears an alkyl group.
  • the octane rating of the unleaded fuel may not be as high.
  • Aromatic amines used in the examples have the following general structure:
  • the unleaded fuel composition also comprises an isoparaffin composition.
  • the unleaded fuel composition comprises about 40 vol. % or more of the isoparaffin composition. In one embodiment, the unleaded fuel composition comprises about 45 vol. % or more of the isoparaffin composition. In one embodiment, the unleaded fuel composition comprises about 50 vol. % or more of the isoparaffin composition.
  • the unleaded fuel composition comprises about 80 vol. % or less of the isoparaffin composition. In one embodiment, the unleaded fuel composition comprises from about 70 vol. % or less of the isoparaffin composition. In one embodiment, the unleaded fuel composition comprises about 60 vol. % or less of the isoparaffin composition.
  • Suitable isoparaffin compositions comprise alkylate, a combination of isoparaffins, and combinations thereof.
  • the isoparaffin composition comprises alkylate.
  • alkylate typically refers to branched-chain paraffin.
  • the branched-chain paraffin typically is derived from the reaction of isoparaffin with olefin. Alkylation is described, for example, in J. Gary, et al. Petroleum Refining, Technology and Economics (2d Ed. 1984) Chapter 10, pp. 159-183, and in Kirk Othmer. Concise Encyclopedia of Chemical Technology (4 th Ed. 1999) Vol. 1, p. 75-76. Both of the foregoing references are incorporated herein by reference.
  • alkylate refers to hydrocarbon compositions used for fuel applications (a) having at least 55 normalized vol. % C5-C10 iso-paraffins measured pursuant to ASTM test method D-6730-01 (2001), or having at least 55 vol. % C5-C10 iso-paraffins measured pursuant to ASTM test method D-6733-01 (2001).
  • ASTM test method D-6730-01 2001
  • ASTM test method D-6733-01 2001
  • the alkylate is a refinery grade alkylate formed by the reaction of a C3-C5 stream with isobutene.
  • the alkylate advantageously comprises about 70 vol. % or more isoparaffins having a total of 8 carbon atoms.
  • the alkylate advantageously comprises greater than 70 vol. % isoparaffins having a total of 8 carbon atoms.
  • the alkylate advantageously comprises about 73 vol. % or more isoparaffins having a total of 8 carbon atoms.
  • the alkylate comprises about 90 vol. % or less isoparaffins having a total of 8 carbon atoms.
  • the alkylate comprises about 85 vol. % or less isoparaffins.
  • the alkylate comprises less than 5 vol. % isoparaffins having a total of 6-7 carbon atoms.
  • Suitable alkylate typically has a RON of, for example, from about 90 to about 95.
  • Suitable alkylate typically has a MON of, for example, from about 88 to about 95.
  • Suitable alkylate typically has an octane rating of, for example, from about 90 to about 95.
  • Suitable alkylates can be obtained from a variety of sources, including Solvents & Chemicals, Pearland, Tex.; Equistar Chemicals; and, Texas Petrochemicals.
  • the isoparaffin composition comprises a combination of isoparaffins.
  • Suitable isoparaffins have the following general structure:
  • R 6 , R 7 , R 8 , R 9 , R 10 , and R 11 independently are selected from the group consisting of hydrogen and alkyl groups having from about 1 to about 7 carbon atoms, provided that the total number of carbon atoms is 11 or less. In one embodiment, R 6 , R 7 , R 8 , R 9 , R 10 , and R 11 independently are selected from the group consisting of hydrogen and methyl groups.
  • the unleaded fuel comprises a combination of iso-pentane and iso-octane. In another advantageous embodiment, the unleaded fuel composition comprises primarily trimethyl pentane. In one embodiment, the unleaded fuel composition comprises primarily 2,2,4-trimethyl pentane.
  • the isoparaffins are commercially available from a variety of sources and/or may be made by known processes. Examples of suitable preparations are described in F. L. Howard, et al. J. Res. Nat. Bur. Standards Research Paper RP 1779, Vol. 38 (March 1947) pp. 365-395, incorporated herein by reference. The isoparaffins made by the above processes may be used as a blend or purified further.
  • the isoparaffins may be obtained by fractional distillation of refinery streams, e.g., straight run gasolines, or alkylation products.
  • Other known methods of making the isoparaffins include, for example, reaction of alkyl metallic compounds (Grignard reagents) with carbonyl compounds, such as aldehydes, ketones, esters, or anhydrides, to form branched chain carbinols, which are dehydrated to the corresponding olefin and thereafter hydrogenated to the alkane.
  • alkyl metallic compounds such as aldehydes, ketones, esters, or anhydrides
  • the unleaded fuel composition optionally comprises oxygenate octane booster.
  • the oxygenate octane booster may be any liquid organic molecule containing one or more alkyl group and one or more oxygen atom. Suitable oxygenate octane boosters include, for example, ethers and alcohols.
  • the oxygenate octane booster is one or more alkyl ether.
  • the alkyl ether comprises an alkyl group having from 1 to 6 carbon atoms.
  • the alkyl group has from 3 to 6 carbon atoms.
  • the alkyl group is a branched chain alkyl group having from 3 to 6 carbon atoms.
  • the alkyl group is a tertiary alkyl group having from 4 to 6 carbon atoms. Suitable tertiary alkyl groups include, for example, tert-butyl groups and tert-amyl groups.
  • the alkyl ether is dialkyl ether. In one embodiment, the alkyl ether is asymmetric dialkyl ether. In one embodiment, the dialkyl ether comprises a tertiary alkyl group and a second alkyl group having from 1 to 6 carbon atoms. In one embodiment, the dialkyl ether comprises a first tertiary alkyl group and second alkyl group having from 1 to 3 carbon atoms. In one embodiment, the second alkyl group is a linear alkyl group. In one embodiment, the second alkyl group is selected from the group consisting of a methyl group and an ethyl group. Specific examples of suitable alkyl ethers include methyl tertiary butyl ether (MTBE), ethyl tertiary butyl ether, and methyl tertiary amyl ether.
  • MTBE methyl tertiary butyl ether
  • ethyl tertiary butyl ether
  • the use of an oxygenate octane booster in the unleaded fuel composition is optional.
  • the unleaded fuel composition may comprise, for example, 25 vol. % or less oxygenate octane booster. In one embodiment, the unleaded fuel composition comprises about 20 vol. % or less oxygenate octane booster. In one embodiment, the unleaded fuel composition comprises about 16 vol. % or less oxygenate octane booster. In one embodiment, the unleaded fuel composition comprises about 8 vol. % or more oxygenate octane booster. In one embodiment, the unleaded fuel composition comprises about 10 vol. % or more oxygenate octane booster. In another embodiment, the unleaded fuel composition comprises about 12 vol. % or more oxygenate octane booster.
  • Suitable oxygenate octane boosters are made using known processes and are available commercially from a variety of sources.
  • the unleaded fuel composition optionally may comprise a variety of other components as long as they are suitable for combustion in an automotive spark ignition engine and they do not have a significant impact on octane number.
  • a component does not have a significant impact on octane number if, in the concentration(s) employed, the octane number is not raised or lowered by more than about 1.0 unit, as calculated by ASTM D-2699-04a (2004), incorporated herein by reference.
  • Suitable components include, for example, motor gasoline additives as listed in ASTM D-4814-04, incorporated herein by reference, or as specified by a regulatory body, e.g., U.S. California Air Resources Board (CARB) or the U.S. Environmental Protection Agency (EPA).
  • CARB U.S. California Air Resources Board
  • EPA U.S. Environmental Protection Agency
  • Examples of other components suitable for use in the unleaded fuel composition include other paraffins, aromatic hydrocarbons, alcohols, ethers, and/or esters.
  • Refinery streams that may be used in the unleaded fuel include, for example, distillation products and reaction products from a refinery such as catalytic reformate, heavy catalytic cracked spirit, light catalytic cracked spirit, straight run gasoline, isomerate, light reformate, light hydrocrackate, and naphtha.
  • Other gasoline components include olefins (in particular with one double bond per molecule). Examples include liquid alkene having from 5 to 10 carbon atoms. In one embodiment, the liquid alkene has from 6 to 8 carbon atoms. The liquid alkene may be linear or branched. Specific examples of suitable liquid alkenes include pentene, isopentene, hexene, isohexene, heptene, and mixtures thereof.
  • paraffins examples include, for example, straight-chain paraffins and cyclic paraffins.
  • Straight chain paraffins are sometimes also referred to as normal paraffins.
  • the fuel also may contain lead replacement additives and/or other common additives which have no significant impact on octane value, for example, dyes, deicing agents, agents for preventing exhaust valve seat wear, anti-oxidants, corrosion inhibitors, anti-static additives, detergents and the like.
  • lead replacement additives and/or other common additives which have no significant impact on octane value, for example, dyes, deicing agents, agents for preventing exhaust valve seat wear, anti-oxidants, corrosion inhibitors, anti-static additives, detergents and the like.
  • the unleaded fuel composition may not comprise any additive.
  • the unleaded fuel composition also may comprise one or more additives.
  • the unleaded fuel composition typically comprises about 1000 ppm or less total amount of additives.
  • each additive typically is present in an amount of about 0.1 ppm or more.
  • each additive is present in an amount of about 0.5 ppm or more.
  • each additive is present in an amount of about 1 ppm or more.
  • each additive is present in an amount of 100 ppm or less.
  • each additive is present in an amount of 50 ppm or less.
  • each additive is present in an amount of 20 ppm or less.
  • the unleaded fuel composition comprises lead replacement additive. In one embodiment, the unleaded fuel composition comprises antioxidant. In one embodiment, the unleaded fuel composition comprises detergent additive. In one embodiment, the unleaded fuel composition comprises a combination of lead replacement additive, antioxidant, and detergent additive.
  • the unleaded fuel composition typically comprises, for example, about 20 mg/kg or more lead replacement additive. In one embodiment, the unleaded fuel composition comprises from about 25 mg/kg or more lead replacement additive. In one embodiment, the unleaded fuel composition comprises about 30 mg/kg or more lead replacement additive. In one embodiment, the unleaded fuel composition comprises about 60 mg/kg or less lead replacement additive. In one embodiment, the unleaded fuel composition comprises about 55 mg/kg or less lead replacement additive. In one embodiment, the unleaded fuel composition comprises about 50 mg/kg or less lead replacement additive.
  • the unleaded fuel composition typically comprises, for example, about 10 mg/kg or more antioxidant. In one embodiment, the unleaded fuel composition comprises about 15 mg/kg or more antioxidant. In one embodiment, the unleaded fuel composition comprises about 20 mg/kg or more antioxidant. In one embodiment, the unleaded fuel composition comprises about 50 mg/kg or less antioxidant. In one embodiment, the unleaded fuel composition comprises about 45 mg/kg or less antioxidant. In one embodiment, the unleaded fuel composition comprises about 40 mg/kg or less antioxidant.
  • the unleaded fuel composition typically comprises, for example, about 0.05 g/gallon or more detergent additive. In one embodiment, the unleaded fuel composition comprises about 0.08 g/gallon or more detergent additive. In one embodiment, the unleaded fuel composition comprises about 0.1 g/gallon or more detergent additive. In one embodiment, the unleaded fuel composition comprises about 4 g/gallon or less detergent additive. In one embodiment, the unleaded fuel composition comprises about 3.5 g/gallon or less detergent additive. In one embodiment, the unleaded fuel composition comprises about 3 g/gallon or less detergent additive.
  • the unleaded fuel composition comprises: about 40 mg/kg lead replacement additive; about 30 mg/kg antioxidant; and, from about 1 to about 2 g/gallon detergent additive.
  • Suitable additives are made using known processes and are available commercially from a variety of sources.
  • the unleaded fuel composition comprises: a combination of alkylated benzenes; greater than 5 vol. % of one or more aromatic amines; and, an isoparaffin composition selected from the group consisting of alkylate, a combination of isoparaffins having a total number of carbon atoms of 11 or less, and combinations thereof.
  • the unleaded fuel composition comprises: from about 20 vol. % to about 60 vol. % of the combination of alkylated benzenes; from greater than 5 vol. % to about 15 vol. % of the one or more aromatic amine; and, from about 40 vol. % to about 80 vol. % of the isoparaffin composition.
  • the unleaded fuel composition comprises greater than 5 vol. % of the aromatic amine.
  • the unleaded fuel composition comprises about 7 vol. % or more of the aromatic amine.
  • the unleaded fuel composition comprises about 10 vol. % or less of the aromatic amine.
  • the unleaded fuel composition comprises about 7 vol. % or less of the aromatic amine.
  • the unleaded fuel composition contains about 7 vol. % of the aromatic amine.
  • the unleaded fuel composition further comprises one or more oxygenate octane booster.
  • the unleaded fuel composition comprises: alkylate; a combination of alkylated benzenes; and, one or more aromatic amines.
  • the unleaded fuel composition comprises: from about 40 vol. % to about 50 vol. % alkylate; from about 30 vol. % to about 40 vol. % toluene; from about 10 vol. % to about 20 vol. % m-xylene; and, from about 2 vol. % to about 12 vol. % aniline.
  • the unleaded fuel composition comprises about 5 vol % or more aniline.
  • the unleaded fuel composition comprises additional additives.
  • the unleaded fuel composition a combination of lead replacement additive, antioxidant, and detergent additive.
  • the unleaded fuel composition also optionally may comprise one or more oxygenate octane booster.
  • Jessup describes fuel compositions having octane ratings of “at least about 100 . . . comprised of toluene and alkylate and at least two further components selected from the group consisting of [isopentane], n-butane and methyl tertiary butyl ether.” Jessup, abstract. Jessup Tables 4 and 7 show ingredients and concentration ranges which meet minimum octane rating requirements of about 100. The highest “Actual Octane Value” that Jessup appears to achieve using the blends is 101. Table 8, Blend #9.
  • U.S. Patent Application 2003/0183554 to R. Bazzani, et al. (“Bazzani”) describes unleaded blend compositions, as well as formulated gasolines containing them, having a Motor Octane Number (MON) of at least 80 comprising a variety of isoparaffin compositions.
  • the composition may comprise at least one aromatic compound, for example having 6-9 carbons, preferably an alkyl aromatic compound such as toluene or o, m, or p xylene or a mixture thereof or a trimethyl benzene.
  • Aromatic amines may be used “in an amount of less than 5% by volume for mogas or avgas, and are preferably substantially absent . . . e.g., less than 100 ppm.” Bazzani, paragraph [0051].
  • Bazzani states with respect to the compositions of Bazzani's “part (a)” that the ROAD value (or octane rating) “is usually 85-115 e.g. 98-115 or preferably 85-98 such as 85-95 e.g. 85-90, or 90-95 or 95-98.
  • Preferred gasoline compositions have . . . ROAD 85-90 . . . ROAD 85-95 or . . . ROAD 90-95.”
  • the highest ROAD value actually reported in the Examples relevant to “part (a)” is 97.25 (Table 1, p. 12).
  • Bazzani states with respect to the compositions in “part (b)” that “the ROAD value is usually 85-107 e.g. 98-106 or preferably 85-98 such as 85-95 e.g. 85-90, or 90-95 or 95-98.
  • Preferred gasoline compositions have . . . ROAD 85-90, or . . . ROAD 85-95 or . . . ROAD 91-96.”
  • Bazzani paragraph [0238]. Although Bazzani states that the compositions of “part (b)” can reach a ROAD value over 105, Bazzani does not state that the compositions tested in the relevant Examples either (a) contained 5 vol.
  • Bazzani states with respect to the compositions in “part (c)” that “the ROAD value is usually 85-110 or 85-107 e.g. 98-106 or 102-108 or 85-95. Preferred gasoline compositions have . . . ROAD 89-96 but especially ROAD 98-106.” Bazzani, paragraph [0342] A ROAD value of 105 is reported for two of the compositions in the Examples relevant to part (c)(Table 23); however, Bazzani does not state that the compositions tested in the relevant Examples either: (a) contained 5 vol. % or more aromatic amine; (b) had a ROAD value of greater than 105; and/or, (c) comprised isoparaffin composition comprising alkylate.
  • Blend 5 the relatively expensive iso-octane and isopentane were replaced with relatively inexpensive alkylate. This embodiment has the advantage of rendering the unleaded fuel composition list costly to produce.
  • a first blend had the following general formula:
  • the RON, MON, and octane rating [R+M)/2] were measured according to ASTM D-2699-04a (RON) and ASTM D-2700-04a (MON)(2004).
  • the RON was 115.67
  • the MON was 106.0
  • the octane number was 110.8.
  • Example 1 The RON was 116.67, the MON was 106.33, and the octane number was 111.5.
  • the foregoing results demonstrate that the formulas of Example 1 and Example 2 are effective to produce an octane number of 110 or more.
  • the RON was 115.0, the MON was 97.5, and the octane number was 106.25.
  • This example illustrates that N-methyl aniline did not produce an octane number of 110 or more, but did produce an octane number of 106 or more.
  • a second blend had the following general formula.
  • the RON was 116.33, the MON was 105.33, and the octane number was 110.8.
  • the RON was 116.00, the MON was 105, and the octane number was 110.5.
  • the RON was 115.0, the MON was 96.93, and the octane number was 106.0.
  • This example illustrates that the use of N-methylaniline as the aromatic amine did not produce an octane number of 110 or more, but did produce an octane number of 106.
  • an oxygenate octane booster such as alkyl ether, is expected to increase the octane number.
  • a third blend had the following general formula.
  • the RON was 117.67
  • the MON was 104.67
  • the octane number was 111.67.
  • a fourth blend had the following general formula.
  • the alkylate had the composition given in the following Table.
  • the numbers in the Table represent the normalized volume %, based on the total volume of the composition, pursuant to ASTM test method D 6730-01, “Standard Test Method for Determination of Individual Components in Spark Ignition Engine Fuels by 100-Metre Capillary (with Precolumn) High-Resolution Gas Chromatography,” incorporated herein by reference:
  • the RON was 118.5, the MON was 101.9, and the octane number was 110.2.
  • a fifth blend had the following general formula.
  • the alkylate had the composition given in the following Table.
  • the numbers in the Table represent volume %, based on the total volume of the composition, pursuant to ASTM test method D 6733-01, “Standard Test Method for Determination of Individual Components in Spark Ignition Engine Fuels by 50-Metre Capillary High-Resolution Gas Chromatography,” incorporated herein by reference:
  • the RON was 114, the MON was 105, and the octane number was 110.

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Abstract

An unleaded fuel composition comprising: a combination of alkylated benzenes comprising alkyl groups having from 1 to 4 carbon atoms; 5 vol. % or more of one or more aromatic amines; and, an isoparaffin composition selected from the group consisting of alkylate, a combination of isoparaffins having a total number of carbon atoms of 11 or less, and combinations thereof.

Description

  • The present application claims the benefit of pending PCT Patent Application No. PCT/US2006/061825, filed Dec. 11, 2006, the entire disclosure of which is hereby incorporated by reference.
  • FIELD OF THE INVENTION
  • The present application relates to unleaded fuel compositions.
  • BACKGROUND OF THE INVENTION
  • In the operation of spark-induced combustion engines, and particularly automotive engines operating on gasoline, the octane rating of the fuel must be high enough to prevent knocking. Gasolines sold at service stations typically have an octane rating of from about 87 to about 93. Fuels having such octane ratings are satisfactory for most automotive engines.
  • For high performance engines, and for racing engines in particular, fuels of even higher octane ratings are required. The production of fuels of progressively higher octane values is progressively more difficult to achieve. In particular, fuels of octane value at or above 100 are highly desired and the most difficult to produce. This is particularly true for unleaded fuels.
  • A need exists for unleaded fuel compositions having high octane ratings.
  • SUMMARY OF THE INVENTION
  • The present application provides unleaded fuel compositions having an octane rating of 105 or more.
  • The present application provides unleaded fuel compositions having an octane rating greater than 105.
  • The present application provides unleaded fuel compositions having an octane rating of 106 or more.
  • The present application also provides unleaded fuel compositions having an octane rating of 110 or more.
  • The present application also provides an unleaded fuel composition comprising: a combination of alkylated benzenes comprising alkyl groups having from 1 to 4 carbon atoms; 5 vol. % or more of one or more aromatic amines; and, an isoparaffin composition selected from the group consisting of alkylate, a combination of isoparaffins having a total number of carbon atoms of 11 or less, and combinations thereof.
  • The present application also provides an unleaded fuel composition comprising: an isoparaffin composition comprising alkylate; a combination of alkylated benzenes comprising alkyl groups having from 1 to 4 carbon atoms; and, one or more aromatic amines comprising an aromatic ring comprising an amine substituent.
  • The present application also provides an unleaded fuel composition comprising: from about 40 vol. % to about 50 vol. % alkylate; from about 30 vol. % to about 40 vol. % toluene; from about 10 vol. % to about 20 vol. % m-xylene; and, from 2 vol. % to about 12 vol. % aniline.
  • The present application also provides an unleaded fuel composition comprising: about 44 vol. % alkylate comprising about 70 vol. % or more isoparaffins having a total of 8 carbon atoms; about 34 vol. % toluene; about 15 vol. % m-xylene; and, about 7 vol. % aniline.
  • DETAILED DESCRIPTION OF THE INVENTION
  • The present application provides unleaded fuel compositions having an octane rating which is higher than typically demonstrated by similar unleaded fuels. Without limiting the invention to a particular theory of operation, the unleaded fuels of the present application comprise aromatic amine, which is believed to contribute to a higher octane rating.
  • It is advantageous for the unleaded fuel compositions to have an octane rating sufficiently high to prevent knocking. In high performance applications, it is advantageous for unleaded fuel compositions to have an octane rating sufficiently high to boost power output from the high performance engine. In one embodiment, the application provides an unleaded racing fuel having an octane rating sufficiently high to boost the power output from a racing engine.
  • The octane rating of a fuel composition generally is calculated as the sum of the Research Octane Number (RON) and the Motor Octane Number (MON) divided by 2, i.e., (R+M)/2. Unless otherwise indicated, the Research Octane Number (RON) is determined according to method ASTM D-2699-04a (2004) and the Motor Octane Number (MON) is determined according to method ASTM D-2700-04a (2004), both incorporated by reference.
  • In one embodiment, the unleaded fuel composition of the present application has an octane rating of about 105 or more. In one embodiment, the unleaded fuel composition has an octane rating of greater than 105. In another embodiment, the unleaded fuel composition of the present application has an octane rating of about 106 or more. In one embodiment, the unleaded fuel composition has an octane rating of about 110 or more.
  • In one embodiment, the unleaded fuel composition comprises: a combination of alkylated benzenes; one or more aromatic amines; and, an isoparaffin composition selected from the group consisting of alkylate, a combination of isoparaffins having a total number of carbon atoms of 11 or less, and combinations thereof.
  • In one embodiment, the unleaded fuel composition comprises: an isoparaffin composition comprising alkylate; a combination of alkylated benzenes; and, one or more aromatic amine. This embodiment has the advantage of being relatively less costly due to the use of isoparaffin composition comprising alkylate.
  • The unleaded fuel composition optionally comprises one or more oxygenate octane booster. The unleaded fuel composition also optionally comprises one or more additional additives.
  • The Alkylated Benzenes
  • The unleaded fuel composition comprises a combination of alkylated benzenes.
  • In one embodiment, the unleaded fuel composition comprises about 20 vol. % or more of a combination of alkylated benzenes. Where used herein, the term “vol. %” is based on the total volume of the unleaded fuel composition, unless otherwise indicated. In one embodiment, the unleaded fuel composition comprises about 25 vol. % or more alkylated benzenes. In yet another embodiment, the unleaded fuel composition comprises about 40 vol. % or more alkylated benzenes.
  • In one embodiment, the unleaded fuel composition comprises about 60 vol. % or less alkylated benzenes. In one embodiment, the unleaded fuel composition comprises about 55 vol. % or less alkylated benzenes. In yet another embodiment, the unleaded fuel composition comprises about 50 vol. % or less alkylated benzenes.
  • Suitable alkylated benzenes have the following general structure:
  • Figure US20080134571A1-20080612-C00001
  • wherein R, R1, and R2 are selected from the group consisting of hydrogen and alkyl groups having from 1 to 4 carbon atoms, provided that at least one of R, R1, and R2 is an alkyl group. In one embodiment, R, R1, and R are selected from the group consisting of hydrogen and alkyl groups having from 1 to 2 carbon atoms. In one embodiment, R, R1, and R2 are selected from the group consisting of hydrogen and methyl groups. In one embodiment, the alkylated benzene is mono-alkylated benzene. In another embodiment, the alkylated benzene is a di-alkylated benzene. In another embodiment, the alkylated benzene is a tri-alkylated benzene. In one embodiment, one or more of R, R1, and R are methyl groups.
  • In an advantageous embodiment, the alkylated benzenes are a combination of mono-alkylated benzene, di-alkylated benzene, and tri-alkylated benzene. In one embodiment, the unleaded fuel composition comprises a combination of monomethyl benzene and dimethyl benzene. In one embodiment, the combination further comprises trimethyl benzene. In one embodiment, the unleaded fuel composition comprises a combination of xylene and toluene. In one embodiment, the unleaded fuel composition further comprises 1,3,5-trimethylbenzene.
  • The Aromatic Amine
  • The unleaded fuel composition also comprises one or more aromatic amine.
  • For lower performance applications, it is possible for the unleaded fuel composition to comprise about 0.1 vol. % or more of one or more aromatic amine. This is particularly true where the isoparaffin comprises the less expensive alkylate. In one embodiment, the unleaded fuel composition comprises about 0.5 vol. % or more of the aromatic amine. In one embodiment, the unleaded fuel composition comprises about 1 vol. % or more of the aromatic amine. In one embodiment, the unleaded fuel composition comprises about 2 vol. % or more of the aromatic amine.
  • In one embodiment, which is particularly advantageous for high performance applications, the unleaded fuel composition comprises 5 vol. % or more of the aromatic amine. In one embodiment, the unleaded fuel composition comprises greater 5 vol. % of the aromatic amine. In one embodiment, the unleaded fuel composition comprises about 6 vol. % or more of the aromatic amine. In another embodiment, the unleaded fuel composition comprises about 7 vol. % or more of the aromatic amine.
  • In one embodiment, the unleaded fuel composition comprises about 15 vol. % or less of the aromatic amine. In one embodiment, the unleaded fuel composition comprises from about 10 vol. % or less of the aromatic amine. In one embodiment, the unleaded fuel composition comprises 8 vol. % or less of the aromatic amine. In one embodiment, the unleaded fuel composition contains about 7 vol. % of the aromatic amine.
  • As used herein, the phrase “aromatic amine” refers to one or more aromatic amines having the following general structure:
  • Figure US20080134571A1-20080612-C00002
  • wherein R3, R4 and R5 independently are selected from the group consisting of hydrogen and alkyl groups having from about 1 to 4 carbon atoms. In one embodiment, R3 is hydrogen. In one embodiment, the alkyl groups have from about 1 to 2 carbon atoms. In one embodiment, the alkyl groups are methyl groups. In one embodiment, R3, R4 and R5 are hydrogens.
  • In one embodiment, the aromatic amine has one or more alkyl substituents on the aromatic ring. In this embodiment, the alkyl group may be at any position relative to the nitrogen containing substituent. In one embodiment, the alkyl group is at a meta-position relative to the nitrogen containing substituent. In one embodiment, the alkyl group is at a para-position relative to the nitrogen containing substituent.
  • In another embodiment, the nitrogen bears an alkyl group. However, where the nitrogen bears an alkyl group, the octane rating of the unleaded fuel may not be as high. Where the nitrogen bears an alkyl group, it may be desirable to include an oxygenate octane booster.
  • Aromatic amines used in the examples have the following general structure:
  • Figure US20080134571A1-20080612-C00003
  • The Isoparaffin Composition
  • The unleaded fuel composition also comprises an isoparaffin composition.
  • In one embodiment, the unleaded fuel composition comprises about 40 vol. % or more of the isoparaffin composition. In one embodiment, the unleaded fuel composition comprises about 45 vol. % or more of the isoparaffin composition. In one embodiment, the unleaded fuel composition comprises about 50 vol. % or more of the isoparaffin composition.
  • In one embodiment, the unleaded fuel composition comprises about 80 vol. % or less of the isoparaffin composition. In one embodiment, the unleaded fuel composition comprises from about 70 vol. % or less of the isoparaffin composition. In one embodiment, the unleaded fuel composition comprises about 60 vol. % or less of the isoparaffin composition.
  • Suitable isoparaffin compositions comprise alkylate, a combination of isoparaffins, and combinations thereof.
  • Alkylate
  • In one embodiment, the isoparaffin composition comprises alkylate. The term “alkylate” typically refers to branched-chain paraffin. The branched-chain paraffin typically is derived from the reaction of isoparaffin with olefin. Alkylation is described, for example, in J. Gary, et al. Petroleum Refining, Technology and Economics (2d Ed. 1984) Chapter 10, pp. 159-183, and in Kirk Othmer. Concise Encyclopedia of Chemical Technology (4th Ed. 1999) Vol. 1, p. 75-76. Both of the foregoing references are incorporated herein by reference.
  • Various grades of branched chain isoparaffins and mixtures are available. The grade is identified by the range of the number of carbon atoms per molecule, the average molecular weight of the molecules, and the boiling point range of the alkylate. As used herein, the word “alkylate” refers to hydrocarbon compositions used for fuel applications (a) having at least 55 normalized vol. % C5-C10 iso-paraffins measured pursuant to ASTM test method D-6730-01 (2001), or having at least 55 vol. % C5-C10 iso-paraffins measured pursuant to ASTM test method D-6733-01 (2001). The foregoing ASTM test methods are incorporated herein by reference.
  • In one embodiment, the alkylate is a refinery grade alkylate formed by the reaction of a C3-C5 stream with isobutene. In this embodiment, the alkylate advantageously comprises about 70 vol. % or more isoparaffins having a total of 8 carbon atoms. In one embodiment, the alkylate advantageously comprises greater than 70 vol. % isoparaffins having a total of 8 carbon atoms. In one embodiment, the alkylate advantageously comprises about 73 vol. % or more isoparaffins having a total of 8 carbon atoms. In one embodiment, the alkylate comprises about 90 vol. % or less isoparaffins having a total of 8 carbon atoms. In yet another embodiment, the alkylate comprises about 85 vol. % or less isoparaffins.
  • In one embodiment, the alkylate comprises less than 5 vol. % isoparaffins having a total of 6-7 carbon atoms.
  • Suitable alkylate typically has a RON of, for example, from about 90 to about 95. Suitable alkylate typically has a MON of, for example, from about 88 to about 95. Suitable alkylate typically has an octane rating of, for example, from about 90 to about 95.
  • Suitable alkylates can be obtained from a variety of sources, including Solvents & Chemicals, Pearland, Tex.; Equistar Chemicals; and, Texas Petrochemicals.
  • Combination of Isoparaffins
  • In one embodiment, the isoparaffin composition comprises a combination of isoparaffins. Suitable isoparaffins have the following general structure:
  • Figure US20080134571A1-20080612-C00004
  • wherein R6, R7, R8, R9, R10, and R11 independently are selected from the group consisting of hydrogen and alkyl groups having from about 1 to about 7 carbon atoms, provided that the total number of carbon atoms is 11 or less. In one embodiment, R6, R7, R8, R9, R10, and R11 independently are selected from the group consisting of hydrogen and methyl groups. In an advantageous embodiment, the unleaded fuel comprises a combination of iso-pentane and iso-octane. In another advantageous embodiment, the unleaded fuel composition comprises primarily trimethyl pentane. In one embodiment, the unleaded fuel composition comprises primarily 2,2,4-trimethyl pentane.
  • The isoparaffins are commercially available from a variety of sources and/or may be made by known processes. Examples of suitable preparations are described in F. L. Howard, et al. J. Res. Nat. Bur. Standards Research Paper RP1779, Vol. 38 (March 1947) pp. 365-395, incorporated herein by reference. The isoparaffins made by the above processes may be used as a blend or purified further.
  • If desired, the isoparaffins may be obtained by fractional distillation of refinery streams, e.g., straight run gasolines, or alkylation products. Other known methods of making the isoparaffins include, for example, reaction of alkyl metallic compounds (Grignard reagents) with carbonyl compounds, such as aldehydes, ketones, esters, or anhydrides, to form branched chain carbinols, which are dehydrated to the corresponding olefin and thereafter hydrogenated to the alkane.
  • Oxygenate Octane Booster
  • The unleaded fuel composition optionally comprises oxygenate octane booster. The oxygenate octane booster may be any liquid organic molecule containing one or more alkyl group and one or more oxygen atom. Suitable oxygenate octane boosters include, for example, ethers and alcohols.
  • In one embodiment, the oxygenate octane booster is one or more alkyl ether. In one embodiment, the alkyl ether comprises an alkyl group having from 1 to 6 carbon atoms. In one embodiment, the alkyl group has from 3 to 6 carbon atoms. In one embodiment, the alkyl group is a branched chain alkyl group having from 3 to 6 carbon atoms. In an advantageous embodiment, the alkyl group is a tertiary alkyl group having from 4 to 6 carbon atoms. Suitable tertiary alkyl groups include, for example, tert-butyl groups and tert-amyl groups.
  • In one embodiment, the alkyl ether is dialkyl ether. In one embodiment, the alkyl ether is asymmetric dialkyl ether. In one embodiment, the dialkyl ether comprises a tertiary alkyl group and a second alkyl group having from 1 to 6 carbon atoms. In one embodiment, the dialkyl ether comprises a first tertiary alkyl group and second alkyl group having from 1 to 3 carbon atoms. In one embodiment, the second alkyl group is a linear alkyl group. In one embodiment, the second alkyl group is selected from the group consisting of a methyl group and an ethyl group. Specific examples of suitable alkyl ethers include methyl tertiary butyl ether (MTBE), ethyl tertiary butyl ether, and methyl tertiary amyl ether.
  • The use of an oxygenate octane booster in the unleaded fuel composition is optional. The unleaded fuel composition may comprise, for example, 25 vol. % or less oxygenate octane booster. In one embodiment, the unleaded fuel composition comprises about 20 vol. % or less oxygenate octane booster. In one embodiment, the unleaded fuel composition comprises about 16 vol. % or less oxygenate octane booster. In one embodiment, the unleaded fuel composition comprises about 8 vol. % or more oxygenate octane booster. In one embodiment, the unleaded fuel composition comprises about 10 vol. % or more oxygenate octane booster. In another embodiment, the unleaded fuel composition comprises about 12 vol. % or more oxygenate octane booster.
  • Suitable oxygenate octane boosters are made using known processes and are available commercially from a variety of sources.
  • Other Components
  • The unleaded fuel composition optionally may comprise a variety of other components as long as they are suitable for combustion in an automotive spark ignition engine and they do not have a significant impact on octane number. A component does not have a significant impact on octane number if, in the concentration(s) employed, the octane number is not raised or lowered by more than about 1.0 unit, as calculated by ASTM D-2699-04a (2004), incorporated herein by reference.
  • Suitable components include, for example, motor gasoline additives as listed in ASTM D-4814-04, incorporated herein by reference, or as specified by a regulatory body, e.g., U.S. California Air Resources Board (CARB) or the U.S. Environmental Protection Agency (EPA).
  • Examples of other components suitable for use in the unleaded fuel composition include other paraffins, aromatic hydrocarbons, alcohols, ethers, and/or esters. Refinery streams that may be used in the unleaded fuel include, for example, distillation products and reaction products from a refinery such as catalytic reformate, heavy catalytic cracked spirit, light catalytic cracked spirit, straight run gasoline, isomerate, light reformate, light hydrocrackate, and naphtha. Other gasoline components include olefins (in particular with one double bond per molecule). Examples include liquid alkene having from 5 to 10 carbon atoms. In one embodiment, the liquid alkene has from 6 to 8 carbon atoms. The liquid alkene may be linear or branched. Specific examples of suitable liquid alkenes include pentene, isopentene, hexene, isohexene, heptene, and mixtures thereof.
  • Examples of other paraffins that may be used in the unleaded fuel include, for example, straight-chain paraffins and cyclic paraffins. Straight chain paraffins are sometimes also referred to as normal paraffins.
  • The fuel also may contain lead replacement additives and/or other common additives which have no significant impact on octane value, for example, dyes, deicing agents, agents for preventing exhaust valve seat wear, anti-oxidants, corrosion inhibitors, anti-static additives, detergents and the like.
  • The unleaded fuel composition may not comprise any additive. The unleaded fuel composition also may comprise one or more additives. Where used, the unleaded fuel composition typically comprises about 1000 ppm or less total amount of additives. Where one or more additives are present, each additive typically is present in an amount of about 0.1 ppm or more. In one embodiment, each additive is present in an amount of about 0.5 ppm or more. In one embodiment, each additive is present in an amount of about 1 ppm or more. In one embodiment, each additive is present in an amount of 100 ppm or less. In one embodiment, each additive is present in an amount of 50 ppm or less. In one embodiment, each additive is present in an amount of 20 ppm or less.
  • In one embodiment, the unleaded fuel composition comprises lead replacement additive. In one embodiment, the unleaded fuel composition comprises antioxidant. In one embodiment, the unleaded fuel composition comprises detergent additive. In one embodiment, the unleaded fuel composition comprises a combination of lead replacement additive, antioxidant, and detergent additive.
  • Where used, the unleaded fuel composition typically comprises, for example, about 20 mg/kg or more lead replacement additive. In one embodiment, the unleaded fuel composition comprises from about 25 mg/kg or more lead replacement additive. In one embodiment, the unleaded fuel composition comprises about 30 mg/kg or more lead replacement additive. In one embodiment, the unleaded fuel composition comprises about 60 mg/kg or less lead replacement additive. In one embodiment, the unleaded fuel composition comprises about 55 mg/kg or less lead replacement additive. In one embodiment, the unleaded fuel composition comprises about 50 mg/kg or less lead replacement additive.
  • Where used, the unleaded fuel composition typically comprises, for example, about 10 mg/kg or more antioxidant. In one embodiment, the unleaded fuel composition comprises about 15 mg/kg or more antioxidant. In one embodiment, the unleaded fuel composition comprises about 20 mg/kg or more antioxidant. In one embodiment, the unleaded fuel composition comprises about 50 mg/kg or less antioxidant. In one embodiment, the unleaded fuel composition comprises about 45 mg/kg or less antioxidant. In one embodiment, the unleaded fuel composition comprises about 40 mg/kg or less antioxidant.
  • Where used, the unleaded fuel composition typically comprises, for example, about 0.05 g/gallon or more detergent additive. In one embodiment, the unleaded fuel composition comprises about 0.08 g/gallon or more detergent additive. In one embodiment, the unleaded fuel composition comprises about 0.1 g/gallon or more detergent additive. In one embodiment, the unleaded fuel composition comprises about 4 g/gallon or less detergent additive. In one embodiment, the unleaded fuel composition comprises about 3.5 g/gallon or less detergent additive. In one embodiment, the unleaded fuel composition comprises about 3 g/gallon or less detergent additive.
  • In a particularly advantageous embodiment, the unleaded fuel composition comprises: about 40 mg/kg lead replacement additive; about 30 mg/kg antioxidant; and, from about 1 to about 2 g/gallon detergent additive.
  • Suitable additives are made using known processes and are available commercially from a variety of sources.
  • Specific Formulations
  • In one embodiment, the unleaded fuel composition comprises: a combination of alkylated benzenes; greater than 5 vol. % of one or more aromatic amines; and, an isoparaffin composition selected from the group consisting of alkylate, a combination of isoparaffins having a total number of carbon atoms of 11 or less, and combinations thereof.
  • In one embodiment, the unleaded fuel composition comprises: from about 20 vol. % to about 60 vol. % of the combination of alkylated benzenes; from greater than 5 vol. % to about 15 vol. % of the one or more aromatic amine; and, from about 40 vol. % to about 80 vol. % of the isoparaffin composition. In one embodiment, the unleaded fuel composition comprises greater than 5 vol. % of the aromatic amine. In one embodiment, the unleaded fuel composition comprises about 7 vol. % or more of the aromatic amine. In one embodiment, the unleaded fuel composition comprises about 10 vol. % or less of the aromatic amine. In one embodiment, the unleaded fuel composition comprises about 7 vol. % or less of the aromatic amine. In one embodiment, the unleaded fuel composition contains about 7 vol. % of the aromatic amine. In one embodiment, the unleaded fuel composition further comprises one or more oxygenate octane booster.
  • In one embodiment, the unleaded fuel composition comprises: alkylate; a combination of alkylated benzenes; and, one or more aromatic amines. In an advantageous embodiment, the unleaded fuel composition comprises: from about 40 vol. % to about 50 vol. % alkylate; from about 30 vol. % to about 40 vol. % toluene; from about 10 vol. % to about 20 vol. % m-xylene; and, from about 2 vol. % to about 12 vol. % aniline. In one embodiment, the unleaded fuel composition comprises about 5 vol % or more aniline.
  • In one embodiment, the unleaded fuel composition comprises additional additives. In one embodiment, the unleaded fuel composition a combination of lead replacement additive, antioxidant, and detergent additive. The unleaded fuel composition also optionally may comprise one or more oxygenate octane booster.
  • Specific examples of suitable blends are given in the following examples, which are illustrative only and should not be construed as limiting the claims:
  • COMPARATIVE EXAMPLE 1
  • U.S. Pat. No. 4,812,146 to Jessup relates to fuels for high performance engines and for racing engines in particular. Jessup describes fuel compositions having octane ratings of “at least about 100 . . . comprised of toluene and alkylate and at least two further components selected from the group consisting of [isopentane], n-butane and methyl tertiary butyl ether.” Jessup, abstract. Jessup Tables 4 and 7 show ingredients and concentration ranges which meet minimum octane rating requirements of about 100. The highest “Actual Octane Value” that Jessup appears to achieve using the blends is 101. Table 8, Blend #9.
  • COMPARATIVE EXAMPLE 2
  • U.S. Patent Application 2003/0183554 to R. Bazzani, et al. (“Bazzani”) describes unleaded blend compositions, as well as formulated gasolines containing them, having a Motor Octane Number (MON) of at least 80 comprising a variety of isoparaffin compositions. The composition may comprise at least one aromatic compound, for example having 6-9 carbons, preferably an alkyl aromatic compound such as toluene or o, m, or p xylene or a mixture thereof or a trimethyl benzene. Aromatic amines may be used “in an amount of less than 5% by volume for mogas or avgas, and are preferably substantially absent . . . e.g., less than 100 ppm.” Bazzani, paragraph [0051].
  • Bazzani states with respect to the compositions of Bazzani's “part (a)” that the ROAD value (or octane rating) “is usually 85-115 e.g. 98-115 or preferably 85-98 such as 85-95 e.g. 85-90, or 90-95 or 95-98. Preferred gasoline compositions have . . . ROAD 85-90 . . . ROAD 85-95 or . . . ROAD 90-95.” Bazzani paragraph [0056]. While Bazzani states that the compositions of “part (a)” can reach a ROAD value over 105, Bazzani does not state that the compositions tested in the relevant Examples either (a) contained 5 vol. % or more aromatic amine, or (b) had a ROAD value of greater than 105. The highest ROAD value actually reported in the Examples relevant to “part (a)” is 97.25 (Table 1, p. 12).
  • Bazzani states with respect to the compositions in “part (b)” that “the ROAD value is usually 85-107 e.g. 98-106 or preferably 85-98 such as 85-95 e.g. 85-90, or 90-95 or 95-98. Preferred gasoline compositions have . . . ROAD 85-90, or . . . ROAD 85-95 or . . . ROAD 91-96.” Bazzani, paragraph [0238]. Although Bazzani states that the compositions of “part (b)” can reach a ROAD value over 105, Bazzani does not state that the compositions tested in the relevant Examples either (a) contained 5 vol. % or more aromatic amine, or (b) had a ROAD value of greater than 105. In fact, the RON and MON values reported in the Examples relevant to part (b) are below 100, and therefore the ROAD value is below 100. Bazzani, pp. 31-34.
  • Bazzani states with respect to the compositions in “part (c)” that “the ROAD value is usually 85-110 or 85-107 e.g. 98-106 or 102-108 or 85-95. Preferred gasoline compositions have . . . ROAD 89-96 but especially ROAD 98-106.” Bazzani, paragraph [0342] A ROAD value of 105 is reported for two of the compositions in the Examples relevant to part (c)(Table 23); however, Bazzani does not state that the compositions tested in the relevant Examples either: (a) contained 5 vol. % or more aromatic amine; (b) had a ROAD value of greater than 105; and/or, (c) comprised isoparaffin composition comprising alkylate. The compounds for which an octane rating of 105 is reported in Bazzani were made using the relatively expensive isoparaffin composition comprising a combination of “cpd A2” (2,2,3,3-tetramethylbutane) and “cpd A1” (2,2,3,3-tetramethylpentane). Bazzani Table 23 and paragraph [0317].
  • EXPERIMENTAL EXAMPLES
  • Synergies sometimes exist between compounds in fuel compositions which give results for certain properties that would be unexpected from traditional or theoretical methods of estimating that property. A large number of fuel compositions were tested to identify fuel compositions which have synergistic effects so as to yield unleaded fuel compositions having octane ratings of about 105 or more. Five unleaded fuel compositions (Blends 1-5) exhibited synergistic effects resulting in octane ratings of about 110 or more.
  • The blends tested had the following fuel components: Iso-octane=2,2,4-trimethylpentane; Iso-pentane=2-methylbutane; EtBE=Ethyl t-butyl ether (t=tertiary); toluene; m-xylene=3-methyltoluene or 1,3-dimethylbenzene; Aromatic amine=Aniline, N-methylaniline, 4-ethylaniline, and m-toluidine (3-methylaniline). In several of the tested blends, including Blend 5, the relatively expensive iso-octane and isopentane were replaced with relatively inexpensive alkylate. This embodiment has the advantage of rendering the unleaded fuel composition list costly to produce.
  • EXAMPLE 1
  • A first blend had the following general formula:
  • Blend 1
  • Component Vol. %
    Iso-octane 45–50%
    Toluene 14–18%
    m-Xylene 12–16%
    Iso-pentane 3–7%
    1,3,5-trimethylbenzene 12–16%
    Aromatic Amine  5–10%
  • The following formula within “Blend 1” was prepared and the octane number was determined:
  • Component Vol. %
    Iso-octane 45.5%  
    Toluene 15%
    m-Xylene 14%
    Iso-pentane 4.5% 
    1,3,5-trimethylbenzene 14%
    Aniline  7%
  • In all of the examples, the RON, MON, and octane rating [R+M)/2] were measured according to ASTM D-2699-04a (RON) and ASTM D-2700-04a (MON)(2004). For the foregoing blend, the RON was 115.67, the MON was 106.0, and the octane number was 110.8.
  • EXAMPLE 2
  • The following formula within “Blend 1” was prepared and the octane number was determined:
  • Component Vol. %
    Iso-octane 45.5%  
    Toluene 15%
    m-Xylene 14%
    Iso-pentane 4.5% 
    1,3,5-trimethylbenzene 14%
    m-toluidine  7%
  • The RON was 116.67, the MON was 106.33, and the octane number was 111.5. The foregoing results demonstrate that the formulas of Example 1 and Example 2 are effective to produce an octane number of 110 or more.
  • EXAMPLE 3
  • The following formula within “Blend 1” was prepared and the octane number was determined:
  • Component Vol. %
    Iso-octane 45.5%  
    Toluene 15%
    m-Xylene 14%
    Iso-pentane 4.5% 
    1,3,5-trimethylbenzene 14%
    N-methylaniline  7%
  • The RON was 115.0, the MON was 97.5, and the octane number was 106.25. This example illustrates that N-methyl aniline did not produce an octane number of 110 or more, but did produce an octane number of 106 or more. Addition of an oxygenate booster, such as alkyl ether, is expected to increase the octane number.
  • Blend 2
  • A second blend had the following general formula.
  • Component Vol. %
    Iso-octane 45–50%
    Toluene 21–26%
    m-Xylene 19–24%
    Iso-pentane  3–7%
    Aromatic Amine  5–10%
  • Examples 4, 5 and 6 fall within “Blend 2.”
  • EXAMPLE 4
  • The following formula within “Blend 2” was prepared and the octane number was determined:
  • Component Vol. %
    Iso-octane 45.5%  
    Toluene 23%
    m-Xylene 21%
    Iso-pentane 3.5% 
    Aniline  7%
  • The RON was 116.33, the MON was 105.33, and the octane number was 110.8.
  • EXAMPLE 5
  • The following formula within “Blend 2” was prepared and the octane number was determined:
  • Component Vol. %
    Iso-octane 45.5%  
    Toluene 23%
    m-Xylene 21%
    Iso-pentane 3.5% 
    m-toluidine  7%
  • The RON was 116.00, the MON was 105, and the octane number was 110.5.
  • EXAMPLE 6
  • The following formula within “Blend 2” was prepared and the octane number was determined:
  • Component Vol. %
    Iso-octane 45.5%  
    Toluene 23%
    m-Xylene 21%
    Iso-pentane 3.5% 
    N-methylaniline  7%
  • The RON was 115.0, the MON was 96.93, and the octane number was 106.0. This example illustrates that the use of N-methylaniline as the aromatic amine did not produce an octane number of 110 or more, but did produce an octane number of 106. Once again, the use of an oxygenate octane booster, such as alkyl ether, is expected to increase the octane number.
  • EXAMPLE 7
  • A third blend had the following general formula.
  • Blend 3
  • Component Vol. %
    Iso-octane 40–49%
    Toluene 13–17%
    m-Xylene 12–16%
    Iso-pentane  3–10%
    EtBE 12–16%
    Aromatic Amine  5–10%
  • The following formula within “Blend 3” was prepared and the octane number was determined:
  • Component Vol. %
    Iso-octane 40.5%  
    Toluene 15%
    m-Xylene 14%
    Iso-pentane 9.5% 
    EtBE 14%
    Aniline  7%
  • The RON was 117.67, the MON was 104.67, and the octane number was 111.67.
  • EXAMPLE 8
  • A fourth blend had the following general formula.
  • Blend 4
  • Component Vol. %
    Toluene 13–17%
    m-Xylene 12–16%
    Alkylate 47–56%
    EtBE 12–16%
    Aromatic Amine  5–10%
  • The following formula within “Blend 4” was prepared and the octane number was determined.
  • Component Vol. %
    Toluene 15%
    m-Xylene 14%
    Alkylate 50.0%  
    EtBE 14%
    Aniline  7%
  • The alkylate had the composition given in the following Table. The numbers in the Table represent the normalized volume %, based on the total volume of the composition, pursuant to ASTM test method D 6730-01, “Standard Test Method for Determination of Individual Components in Spark Ignition Engine Fuels by 100-Metre Capillary (with Precolumn) High-Resolution Gas Chromatography,” incorporated herein by reference:
  • Number of Normal
    carbon atoms Naphthene Iso-paraffins paraffins Aromatics
    4 0.36
    5 4.07
    6 3.79
    7 3.93 0.07
    8 27.41 54.17
    9 1.73
    10  0.53
    11  0.70
    boiling 3.24
    point >200° C.
  • The RON was 118.5, the MON was 101.9, and the octane number was 110.2.
  • EXAMPLE 9
  • A fifth blend had the following general formula.
  • Blend 5
  • Component Vol. %
    Toluene 30–40%
    m-Xylene 10–20%
    Alkylate 40–50%
    Aromatic Amine  2–12%
  • The following formula within “Blend 5” was prepared and the octane number was determined.
  • Component Vol. %
    Toluene 34%
    m-Xylene 15%
    Alkylate 44%
    Aniline  7%
  • The alkylate had the composition given in the following Table. The numbers in the Table represent volume %, based on the total volume of the composition, pursuant to ASTM test method D 6733-01, “Standard Test Method for Determination of Individual Components in Spark Ignition Engine Fuels by 50-Metre Capillary High-Resolution Gas Chromatography,” incorporated herein by reference:
  • Number of
    carbon iso- normal
    atoms Naphthene paraffins paraffins aromatics
    4 1.01 3.75
    5 10.47 0.18
    6 0.01 1.27 0.02
    7 1.96
    8 0.10 73.50
    9 0.30 1.80
    10 2.41 0.02
    11 2.79
  • The RON was 114, the MON was 105, and the octane number was 110.
  • Persons of ordinary skill in the art will recognize that many modifications may be made to the foregoing description. The embodiments described herein are meant to be illustrative only and should not be taken as limiting the invention, which will be defined in the claims.

Claims (51)

1. An unleaded fuel composition comprising:
a combination of alkylated benzenes comprising alkyl groups having from 1 to 4 carbon atoms;
5 vol. % or more of one or more aromatic amines; and,
an isoparaffin composition selected from the group consisting of alkylate, a combination of isoparaffins having a total number of carbon atoms of 11 or less, and combinations thereof.
2. The unleaded fuel composition of claim 1 having an octane number of greater than 105.
3. The unleaded fuel composition of claim 1 having an octane number of 106 or more.
4. The unleaded fuel composition of claim 1 having an octane number of 110 or more.
5. The unleaded fuel composition of claim 4 wherein the composition is free of any other ingredient or combination of ingredients which increases the octane number of the fuel composition by more than 1.0 unit.
6. The unleaded fuel composition of claim 1 further comprising one or more oxygenate octane boosters.
7. The unleaded fuel composition of claim 5 further comprising one or more oxygenate octane boosters.
8. The unleaded fuel composition of claim 7 wherein the one or more oxygenate octane boosters comprise alkyl ethers selected from the group consisting of methyl tertiary butyl ether, ethyl tertiary butyl ether, and methyl tertiary amyl ether.
9. The unleaded fuel composition of claim 1 wherein the alkylated benzenes comprise alkyl groups having from 1 to 2 carbon atoms.
10. The unleaded fuel composition of claim 9 wherein the alkyl groups are methyl groups.
11. The unleaded fuel composition of claim 1 wherein the one or more aromatic amines have the following structure:
Figure US20080134571A1-20080612-C00005
wherein R3, R4, and R5 independently are selected from the group consisting of hydrogen and alkyl groups having from about 1 to 2 carbon atoms.
12. The unleaded fuel composition of claim 11 wherein R3, R4, and R5 independently are selected from the group consisting of hydrogen and methyl groups.
13. The unleaded fuel composition of claim 11 wherein R3 is hydrogen.
14. The unleaded fuel composition of claim 11 wherein R4 is hydrogen and R5 is an alkyl group located at a position relative to the —HNR3 group selected from the group consisting of the meta-position and the para-position.
15. The unleaded fuel composition of claim 13 wherein R4 is hydrogen and R5 is an alkyl group located at a position relative to the —HNR3 group selected from the group consisting of the meta-position and the para-position.
16. The unleaded fuel composition of claim 15 comprising:
from about 20 vol. % to about 60 vol. % of the combination of alkylated benzenes;
about 15 vol. % or less of the one or more aromatic amines; and,
from about 40 vol. % to about 80 vol. % of the isoparaffin composition.
17. The unleaded fuel composition of claim 15 comprising:
from about 14 vol. % to about 18 vol. % toluene;
from about 12 vol. % to about 16 vol. % m-xylene; and,
from about 12 vol. % to about 16 vol. % 1,3,5-trimethylbenzene;
from about 45 vol. % to about 50 vol. % isooctane;
from about 3 vol. % to about 7 vol. % iso-pentane; and,
from about 5 vol. % to about 10 vol. % of the one or more aromatic amines.
18. The unleaded fuel composition of claim 15 comprising:
from about 40 vol. % to about 50 vol. % of the combination of alkylated benzenes;
from about 45 vol. % to about 50 vol. % isooctane;
from about 3 vol. % to about 7 vol. % iso-pentane; and,
from about 5 vol. % to about 10 vol. % of the one or more aromatic amines.
19. The unleaded fuel composition of claim 18 wherein the combination of alkylated benzenes comprises:
from about 21 vol. % to about 25 vol. % toluene; and
from about 19 vol. % to about 24 vol. % m-xylene, based on the total weight of the unleaded fuel composition.
20. The unleaded fuel composition of claim 15 comprising:
from about 13 vol. % to about 17 vol. % toluene;
from about 12 vol. % to about 16 vol. % m-xylene;
from about 12 vol. % to about 16 vol. % 1,3,5-trimethylbenzene;
from about 3 vol. % to about 10 vol. % iso-pentane;
from about 40 vol. % to about 49 vol. % isooctane;
from about 5 vol. % to about 10 vol. % of the one or more aromatic amines; and,
from about 12 vol. % to about 16 vol. % of an oxygenate octane booster comprising one or more alkyl ethers.
21. The unleaded fuel composition of claim 15 comprising:
from about 13 vol. % to about 17 vol. % toluene;
from about 12 vol. % to about 16 vol. % m-xylene;
from about 47 vol. % to about 56 vol. % alkylate;
from about 5 vol. % to about 10 vol. % of the one or more aromatic amines; and,
from about 12 vol. % to about 16 vol. % of an oxygenate octane booster comprising one or more alkyl ethers.
22. An unleaded fuel composition comprising:
an isoparaffin composition comprising alkylate;
a combination of alkylated benzenes comprising alkyl groups having from 1 to 4 carbon atoms; and,
one or more aromatic amines comprising an aromatic ring comprising an amine substituent.
23. The unleaded fuel composition of claim 22 comprising about 0.1 vol. % or more of the one or more aromatic amines.
24. The unleaded fuel composition of claim 22 comprising about 0.5 vol. % or more of the one or more aromatic amines.
25. The unleaded fuel composition of claim 22 comprising about 1 vol. % or more of the one or more aromatic amines.
26. The unleaded fuel composition of claim 22 comprising about 2 vol. % or more of one or more aromatic amines.
27. The unleaded fuel composition of claim 22 comprising 5 vol. % or more of the one or more aromatic amines.
28. The unleaded fuel composition of claim 27 wherein the one or more aromatic amines comprise an alkyl substituent at a position relative to the amine substituent selected from the group consisting of the meta-position and the para-position.
29. The unleaded fuel composition of claim 28 wherein the amine substituent is a —NH2 substituent.
30. The unleaded fuel composition of claim 22 wherein the isoparaffin composition is alkylate.
31. The unleaded fuel composition of claim 29 wherein the isoparaffin composition is alkylate.
32. The unleaded fuel composition of claim 22 having an octane number of 105 or more.
33. The unleaded fuel composition of claim 29 having an octane number of 105 or more.
34. The unleaded fuel composition of claim 22 having an octane number of 110 or more.
35. The unleaded fuel composition of claim 29 having an octane number of 110 or more.
36. The unleaded fuel composition of claim 22 wherein the alkylate comprises about 70 vol. % or more isoparaffins having a total of 8 carbon atoms.
37. The unleaded fuel composition of claim 34 wherein the composition is free of any other ingredient or combination of ingredients which increases the octane number of the fuel composition by more than 1.0 unit.
38. The unleaded fuel composition of claim 22 further comprising one or more oxygenated octane boosters.
39. The unleaded fuel composition of claim 38 wherein the one or more oxygenated octane boosters comprise alkyl ethers selected from the group consisting of methyl tertiary butyl ether, ethyl tertiary butyl ether, and methyl tertiary amyl ether.
40. The unleaded fuel composition of claim 22 wherein
the alkylated benzenes comprise alkyl groups having from 1 to 2 carbon atoms; and,
the one or more aromatic amines have the following structure:
Figure US20080134571A1-20080612-C00006
wherein R3, R4, and R5 independently are selected from the group consisting of hydrogen and alkyl groups having from about 1 to 2 carbon atoms.
41. The unleaded fuel composition of claim 40 wherein R3, R4, and R5 independently are selected from the group consisting of hydrogen and alkyl groups having 1 carbon atom.
42. The unleaded fuel composition of claim 40 wherein R3 is hydrogen.
43. The unleaded fuel composition of claim 40 wherein R4 is hydrogen and R5 is an alkyl group located at a position relative to the —HNR3 group selected from the group consisting of the meta-position and the para-position.
44. The unleaded fuel composition of claim 42 wherein R4 is hydrogen and R5 is an alkyl group located at a position relative to the —HNR3 group selected from the group consisting of the meta-position and the para-position.
45. The unleaded fuel composition of claim 43 comprising:
from about 40 vol. % to about 60 vol. % of the combination of alkylated benzenes;
about 15 vol. % or less of the one or more aromatic amines; and,
from about 40 vol. % to about 50 vol. % alkylate.
46. An unleaded fuel composition comprising:
from about 40 vol. % to about 50 vol. % alkylate;
from about 30 vol. % to about 40 vol. % toluene;
from about 10 vol. % to about 20 vol. % m-xylene; and,
from 2 vol. % to about 12 vol. % aniline.
47. The unleaded fuel composition of claim 46 comprising about 5 vol. % or more aniline.
48. The unleaded fuel composition of claim 46 comprising:
from about 42 vol. % to about 46 vol. % alkylate;
from about 32 vol. % to about 36 vol. % toluene;
from about 13 vol. % to about 17 vol. % m-xylene; and,
from about 5 vol. % to about 9 vol. % aniline.
49. The unleaded fuel composition of claim 46 wherein the alkylate comprises about 70 vol. % or more isoparaffins having a total of 8 carbon atoms.
50. An unleaded fuel composition comprising:
about 44 vol. % alkylate comprising about 70 vol. % or more isoparaffins having a total of 8 carbon atoms;
about 34 vol. % toluene;
about 15 vol. % m-xylene; and,
about 7 vol. % aniline.
51. The unleaded fuel composition of claim 50 further comprising:
40 mg/kg lead replacement additive;
30 mg/kg antioxidant; and,
from about 1 to about 2 g/gallon detergent additive.
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Cited By (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20100018112A1 (en) * 2008-07-28 2010-01-28 Joseph Michael Russo High octane unleaded fuel compositions and methods for increasing the maximum torque output value produced burning same
WO2012015506A1 (en) * 2010-07-28 2012-02-02 Chevron U.S.A. Inc. High octane aviation fuel composition
US20120279112A1 (en) * 2009-11-23 2012-11-08 Chimec S.P.A. High octane number composition useful as fuel for internal combustion and controlled ignition engine
EP2576737A1 (en) * 2010-05-26 2013-04-10 Swift Fuels, LLC Biogenic turbine and dieselfuel
US8628594B1 (en) * 2009-12-01 2014-01-14 George W. Braly High octane unleaded aviation fuel
US20140116367A1 (en) * 2009-12-01 2014-05-01 George W. Braly High octane unleaded aviation gasoline
US20140123548A1 (en) * 2009-12-01 2014-05-08 George W. Braly High octane unleaded aviation gasoline
US8840689B2 (en) 2011-08-30 2014-09-23 Johann Haltermann Limited Aviation gasoline
GB2515200A (en) * 2013-10-31 2014-12-17 Shell Int Research High octane unleaded aviation gasoline
GB2515198A (en) * 2013-10-31 2014-12-17 Shell Int Research High octane unleaded aviation gasoline
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GB2515202A (en) * 2013-10-31 2014-12-17 Shell Int Research High octane unleaded aviation gasoline
GB2516769A (en) * 2013-10-31 2015-02-04 Shell Int Research High octane unleaded aviation gasoline
GB2518731A (en) * 2013-10-31 2015-04-01 Shell Int Research High octane unleaded aviation gasoline
US20150175918A1 (en) * 2013-12-09 2015-06-25 Swift Fuels, Llc Aviation gasolines containing mesitylene and isopentane
US9074153B2 (en) 2006-12-12 2015-07-07 Shell Oil Company Unleaded fuel compositions
US9163189B2 (en) 2011-12-01 2015-10-20 Shell Oil Company Balanced unleaded fuel compositions
WO2016016336A1 (en) * 2014-07-29 2016-02-04 Chemieanlagenbau Chemnitz Gmbh Synthetic gasoline and use thereof
EP3109297A1 (en) * 2015-06-25 2016-12-28 Shell Internationale Research Maatschappij B.V. Fuel formulations
EP3169755A4 (en) * 2014-07-14 2018-02-14 Swift Fuels, LLC Aviation fuel with a renewable oxygenate
WO2018122691A1 (en) * 2016-12-28 2018-07-05 Sabic Global Technologies B.V. Lead-free, oxygenated, high-octane gasoline blend
US10294435B2 (en) 2016-11-01 2019-05-21 Afton Chemical Corporation Manganese scavengers that minimize octane loss in aviation gasolines
US10364399B2 (en) 2017-08-28 2019-07-30 General Aviation Modifications, Inc. High octane unleaded aviation fuel
US10377959B2 (en) 2017-08-28 2019-08-13 General Aviation Modifications, Inc. High octane unleaded aviation fuel
WO2021206873A1 (en) * 2020-04-09 2021-10-14 Exxonmobil Research And Engineering Company Fuel blending component composition and method for reducing criteria emissions
US11193077B1 (en) * 2013-03-13 2021-12-07 Airworthy Autogas, Llc Gasoline for aircraft use
US11220648B2 (en) * 2016-11-15 2022-01-11 Exxonmobil Research And Engineering Company Fuel compositions for controlling combustion in engines

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20180037838A1 (en) * 2015-02-27 2018-02-08 Shell Oil Company Use of a lubricating composition

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4812146A (en) * 1988-06-09 1989-03-14 Union Oil Company Of California Liquid fuels of high octane values
US5015356A (en) * 1979-08-29 1991-05-14 Talbert William L Hydrocarbon fuel systems
US5284984A (en) * 1992-12-29 1994-02-08 Mobil Oil Corporation Gasoline upgrading by aromatics amination
US5312542A (en) * 1979-08-29 1994-05-17 Talbert Fuel Systems, Inc Hydrocarbon fuel and fuel systems
US5470358A (en) * 1993-05-04 1995-11-28 Exxon Research & Engineering Co. Unleaded aviation gasoline
US6030521A (en) * 1990-12-13 2000-02-29 Union Oil Company Of California Gasoline fuel
US6353143B1 (en) * 1998-11-13 2002-03-05 Pennzoil-Quaker State Company Fuel composition for gasoline powered vehicle and method
US20020045785A1 (en) * 1996-11-18 2002-04-18 Bazzani Roberto Vittorio Fuel composition
US20020143216A1 (en) * 2001-01-26 2002-10-03 Kazushi Tsurutani Motor gasoline composition
US20030046862A1 (en) * 2001-05-02 2003-03-13 Wolf Leslie R. Method and an unleaded low emission gasoline for fueling an automotive engine with reduced emissions
US20030145514A1 (en) * 2000-03-23 2003-08-07 Takashi Akimoto Fuel oil for use both in internal combustion in engine and fuel cell
US20030183554A1 (en) * 1996-11-18 2003-10-02 Bp Oil International Limited Fuel composition
US20060123696A1 (en) * 2004-11-30 2006-06-15 Gaughan Roger G Unleaded aminated aviation gasoline exhibiting control of toluene insoluble deposits

Family Cites Families (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4247726A (en) 1980-02-21 1981-01-27 Shell Oil Company Para-xylene process and catalyst
EG22450A (en) * 1998-03-26 2003-02-26 Bp Oil Int Fuel composition
US6132479A (en) 1998-05-04 2000-10-17 Chevron U.S.A. Inc. Low emission, non-oxygenated fuel composition
MY137245A (en) 1999-05-26 2009-01-30 Shell Int Research Gasoline composition
GB0022709D0 (en) 2000-09-15 2000-11-01 Bp Oil Int Fuel composition
US7416568B2 (en) 2002-11-14 2008-08-26 Bp Oil International Limited Aviation gasoline composition, its preparation and use
EP1650287B1 (en) 2003-07-04 2012-03-28 Beijing Grand Golden-Bright Engineering & Technologies Co. Ltd. A method for recombining catalytic hydrocarbons
BRPI0404605B1 (en) 2004-10-22 2013-10-15 AVIATION GAS FORMULATION
US7314033B2 (en) 2004-11-18 2008-01-01 Massachusetts Institute Of Technology Fuel management system for variable ethanol octane enhancement of gasoline engines
GB2433265A (en) 2005-12-16 2007-06-20 Derek Lowe Low toxicity fuel
EP2537913A1 (en) 2006-12-11 2012-12-26 Shell Internationale Research Maatschappij B.V. Unleaded fuel compositions
US20080134571A1 (en) 2006-12-12 2008-06-12 Jorg Landschof Unleaded fuel compositions
DE102007035500A1 (en) 2007-07-28 2009-01-29 Andreas Stihl Ag & Co. Kg Fuel composition
US20100018112A1 (en) 2008-07-28 2010-01-28 Joseph Michael Russo High octane unleaded fuel compositions and methods for increasing the maximum torque output value produced burning same
US8628594B1 (en) 2009-12-01 2014-01-14 George W. Braly High octane unleaded aviation fuel

Patent Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5015356A (en) * 1979-08-29 1991-05-14 Talbert William L Hydrocarbon fuel systems
US5312542A (en) * 1979-08-29 1994-05-17 Talbert Fuel Systems, Inc Hydrocarbon fuel and fuel systems
US4812146A (en) * 1988-06-09 1989-03-14 Union Oil Company Of California Liquid fuels of high octane values
US6030521A (en) * 1990-12-13 2000-02-29 Union Oil Company Of California Gasoline fuel
US5284984A (en) * 1992-12-29 1994-02-08 Mobil Oil Corporation Gasoline upgrading by aromatics amination
US5470358A (en) * 1993-05-04 1995-11-28 Exxon Research & Engineering Co. Unleaded aviation gasoline
US20030183554A1 (en) * 1996-11-18 2003-10-02 Bp Oil International Limited Fuel composition
US20020045785A1 (en) * 1996-11-18 2002-04-18 Bazzani Roberto Vittorio Fuel composition
US6353143B1 (en) * 1998-11-13 2002-03-05 Pennzoil-Quaker State Company Fuel composition for gasoline powered vehicle and method
US20030145514A1 (en) * 2000-03-23 2003-08-07 Takashi Akimoto Fuel oil for use both in internal combustion in engine and fuel cell
US20020143216A1 (en) * 2001-01-26 2002-10-03 Kazushi Tsurutani Motor gasoline composition
US20030046862A1 (en) * 2001-05-02 2003-03-13 Wolf Leslie R. Method and an unleaded low emission gasoline for fueling an automotive engine with reduced emissions
US20060123696A1 (en) * 2004-11-30 2006-06-15 Gaughan Roger G Unleaded aminated aviation gasoline exhibiting control of toluene insoluble deposits

Cited By (78)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9074153B2 (en) 2006-12-12 2015-07-07 Shell Oil Company Unleaded fuel compositions
US20100018112A1 (en) * 2008-07-28 2010-01-28 Joseph Michael Russo High octane unleaded fuel compositions and methods for increasing the maximum torque output value produced burning same
US20120279112A1 (en) * 2009-11-23 2012-11-08 Chimec S.P.A. High octane number composition useful as fuel for internal combustion and controlled ignition engine
US8894727B2 (en) * 2009-11-23 2014-11-25 Chimec S.P.A. High octane number composition useful as fuel for internal combustion and controlled ignition engine
US10260016B2 (en) * 2009-12-01 2019-04-16 George W. Braly High octane unleaded aviation gasoline
US20140116367A1 (en) * 2009-12-01 2014-05-01 George W. Braly High octane unleaded aviation gasoline
US11674100B2 (en) * 2009-12-01 2023-06-13 General Aviation Modifications, Inc. High octane unleaded aviation gasoline
US20140123548A1 (en) * 2009-12-01 2014-05-08 George W. Braly High octane unleaded aviation gasoline
US10550347B2 (en) * 2009-12-01 2020-02-04 General Aviation Modifications, Inc. High octane unleaded aviation gasoline
US20200277535A1 (en) * 2009-12-01 2020-09-03 General Aviation Modifications, Inc. High octane unleaded aviation gasoline
US11098259B2 (en) * 2009-12-01 2021-08-24 General Aviation Modifications, Inc. High octane unleaded aviation gasoline
US20220145198A1 (en) * 2009-12-01 2022-05-12 General Aviation Modifications, Inc. High octane unleaded aviation gasoline
US8628594B1 (en) * 2009-12-01 2014-01-14 George W. Braly High octane unleaded aviation fuel
EP2576737A4 (en) * 2010-05-26 2013-12-04 Swift Fuels Llc Biogenic turbine and dieselfuel
EP2576737A1 (en) * 2010-05-26 2013-04-10 Swift Fuels, LLC Biogenic turbine and dieselfuel
AU2011283181B2 (en) * 2010-07-28 2013-09-19 Chevron U.S.A. Inc. High octane aviation fuel composition
JP2013532753A (en) * 2010-07-28 2013-08-19 シェブロン ユー.エス.エー. インコーポレイテッド High octane aviation fuel composition
US8324437B2 (en) 2010-07-28 2012-12-04 Chevron U.S.A. Inc. High octane aviation fuel composition
WO2012015506A1 (en) * 2010-07-28 2012-02-02 Chevron U.S.A. Inc. High octane aviation fuel composition
US8840689B2 (en) 2011-08-30 2014-09-23 Johann Haltermann Limited Aviation gasoline
US9163189B2 (en) 2011-12-01 2015-10-20 Shell Oil Company Balanced unleaded fuel compositions
US11485923B1 (en) 2013-03-13 2022-11-01 Airworthy Autogas, Llc Gasoline for aircraft use
US11193077B1 (en) * 2013-03-13 2021-12-07 Airworthy Autogas, Llc Gasoline for aircraft use
AU2014206202B2 (en) * 2013-10-31 2015-10-15 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
GB2515199B (en) * 2013-10-31 2016-03-23 Shell Int Research High octane unleaded aviation gasoline
EP2868734A1 (en) 2013-10-31 2015-05-06 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
EP2868733A1 (en) 2013-10-31 2015-05-06 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
EP2868738A1 (en) 2013-10-31 2015-05-06 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
EP2868732A1 (en) 2013-10-31 2015-05-06 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
US9035114B1 (en) * 2013-10-31 2015-05-19 Shell Oil Company High octane unleaded aviation gasoline
US20150159106A1 (en) * 2013-10-31 2015-06-11 Shell Oil Company High octane unleaded aviation gasoline
GB2515200A (en) * 2013-10-31 2014-12-17 Shell Int Research High octane unleaded aviation gasoline
US20150175920A1 (en) * 2013-10-31 2015-06-25 Shell Oil Company High octane unleaded aviation gasoline
US20150175921A1 (en) * 2013-10-31 2015-06-25 Shell Oil Company High octane unleaded aviation gasoline
EP2868736A1 (en) 2013-10-31 2015-05-06 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
US9120991B2 (en) 2013-10-31 2015-09-01 Shell Oil Company High octane unleaded aviation gasoline
US9127225B2 (en) 2013-10-31 2015-09-08 Shell Oil Company High octane unleaded aviation gasoline
AU2014206195B2 (en) * 2013-10-31 2015-10-15 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
EP2868737A1 (en) 2013-10-31 2015-05-06 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
AU2014206200B2 (en) * 2013-10-31 2015-10-15 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
US20150113866A1 (en) * 2013-10-31 2015-04-30 Shell Oil Company High octane unleaded aviation gasoline
AU2014206193B2 (en) * 2013-10-31 2015-10-22 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
AU2014206207B2 (en) * 2013-10-31 2015-11-12 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
AU2014206204B2 (en) * 2013-10-31 2015-11-12 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
AU2014206200C1 (en) * 2013-10-31 2016-01-28 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
GB2515198A (en) * 2013-10-31 2014-12-17 Shell Int Research High octane unleaded aviation gasoline
AU2014206202C1 (en) * 2013-10-31 2016-02-18 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
GB2515198B (en) * 2013-10-31 2016-03-23 Shell Int Research High octane unleaded aviation gasoline
GB2515201B (en) * 2013-10-31 2016-03-23 Shell Int Research High Octane Unleaded Aviation Gasoline
GB2515200B (en) * 2013-10-31 2016-03-23 Shell Int Research High octane unleaded aviation gasoline
EP2868735A1 (en) 2013-10-31 2015-05-06 Shell Internationale Research Maatschappij B.V. High octane unleaded aviation gasoline
GB2516769B (en) * 2013-10-31 2016-03-23 Shell Int Research High octane unleaded aviation gasoline
GB2515202B (en) * 2013-10-31 2016-03-23 Shell Int Research High octane unleaded aviation gasoline
GB2518731B (en) * 2013-10-31 2016-03-23 Shell Int Research High octane unleaded aviation gasoline
US9388357B2 (en) * 2013-10-31 2016-07-12 Shell Oil Company High octane unleaded aviation gasoline
US9388358B2 (en) * 2013-10-31 2016-07-12 Shell Oil Company High octane unleaded aviation gasoline
US9388359B2 (en) * 2013-10-31 2016-07-12 Shell Oil Company High octane unleaded aviation gasoline
US9388356B2 (en) * 2013-10-31 2016-07-12 Shell Oil Company High octane unleaded aviation gasoline
GB2515201A (en) * 2013-10-31 2014-12-17 Shell Int Research High Octane Unleaded Aviation Gasoline
GB2515199A (en) * 2013-10-31 2014-12-17 Shell Int Research High octane unleaded aviation gasoline
GB2515202A (en) * 2013-10-31 2014-12-17 Shell Int Research High octane unleaded aviation gasoline
GB2516769A (en) * 2013-10-31 2015-02-04 Shell Int Research High octane unleaded aviation gasoline
US20150113861A1 (en) * 2013-10-31 2015-04-30 Shell Oil Company High octane unleaded aviation gasoline
GB2518731A (en) * 2013-10-31 2015-04-01 Shell Int Research High octane unleaded aviation gasoline
US9816041B2 (en) * 2013-12-09 2017-11-14 Swift Fuels, Llc Aviation gasolines containing mesitylene and isopentane
US20150175918A1 (en) * 2013-12-09 2015-06-25 Swift Fuels, Llc Aviation gasolines containing mesitylene and isopentane
US11407951B2 (en) * 2013-12-09 2022-08-09 Swift Fuels, Llc Aviation gasolines containing mesitylene and isopentane
US10450526B2 (en) 2014-07-14 2019-10-22 Swift Fuels, Llc Aviation fuel with a renewable oxygenate
EP3169755A4 (en) * 2014-07-14 2018-02-14 Swift Fuels, LLC Aviation fuel with a renewable oxygenate
WO2016016336A1 (en) * 2014-07-29 2016-02-04 Chemieanlagenbau Chemnitz Gmbh Synthetic gasoline and use thereof
EP3109297A1 (en) * 2015-06-25 2016-12-28 Shell Internationale Research Maatschappij B.V. Fuel formulations
US10294435B2 (en) 2016-11-01 2019-05-21 Afton Chemical Corporation Manganese scavengers that minimize octane loss in aviation gasolines
US11220648B2 (en) * 2016-11-15 2022-01-11 Exxonmobil Research And Engineering Company Fuel compositions for controlling combustion in engines
WO2018122691A1 (en) * 2016-12-28 2018-07-05 Sabic Global Technologies B.V. Lead-free, oxygenated, high-octane gasoline blend
US10364399B2 (en) 2017-08-28 2019-07-30 General Aviation Modifications, Inc. High octane unleaded aviation fuel
US10377959B2 (en) 2017-08-28 2019-08-13 General Aviation Modifications, Inc. High octane unleaded aviation fuel
WO2021206873A1 (en) * 2020-04-09 2021-10-14 Exxonmobil Research And Engineering Company Fuel blending component composition and method for reducing criteria emissions
US11339338B2 (en) * 2020-04-09 2022-05-24 ExxonMobil Technology and Engineering Company Fuel blending component composition and method for reducing criteria emissions

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