EP1359207A1 - Fuel composition - Google Patents

Fuel composition Download PDF

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Publication number
EP1359207A1
EP1359207A1 EP03076773A EP03076773A EP1359207A1 EP 1359207 A1 EP1359207 A1 EP 1359207A1 EP 03076773 A EP03076773 A EP 03076773A EP 03076773 A EP03076773 A EP 03076773A EP 1359207 A1 EP1359207 A1 EP 1359207A1
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EP
European Patent Office
Prior art keywords
gasoline
composition
total
triptane
volume
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
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EP03076773A
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German (de)
French (fr)
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EP1359207B1 (en
Inventor
Roberto Vittorio Bazzani
Graham Bp Refining Technology Butler
John Hardy Cooper
Paul James Bennett
Alisdair Quentin Clark
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BP Oil International Ltd
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BP Oil International Ltd
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Priority claimed from GBGB9806440.5A external-priority patent/GB9806440D0/en
Priority claimed from GBGB9822277.1A external-priority patent/GB9822277D0/en
Application filed by BP Oil International Ltd filed Critical BP Oil International Ltd
Publication of EP1359207A1 publication Critical patent/EP1359207A1/en
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Publication of EP1359207B1 publication Critical patent/EP1359207B1/en
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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, 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
    • C10L1/04Liquid carbonaceous fuels essentially based on blends of hydrocarbons
    • C10L1/06Liquid carbonaceous fuels essentially based on blends of hydrocarbons for spark ignition

Definitions

  • This invention relates to a fuel composition, in particular a gasoline composition for use in motor vehicles.
  • the present invention provides an unleaded blend composition having a Motor Octane Number (MON) of at least 80 comprising component (a) at least 5% or preferably at least 8 or 10% (by volume of the total composition) of at least one hydrocarbon having the following formula I R-CH 2 -CH(CH 3 )-C(CH 3 ) 2 -CH 3 wherein R is hydrogen or methyl and component (b) at least one saturated liquid aliphatic hydrocarbon having 4 to 12, 4-10 such as 5-10 e.g. 5 - 8 carbon atoms.
  • component (b) is contained in at least one of isomerate, alkylate, straight run gasoline, light reformate, light hydrocrackate and aviation alkylate.
  • the composition comprises at least one of an olefin (e.g. in amount of 1-30%) and/or at least one aromatic hydrocarbon (e.g. in amount of 1-50%, especially 3-28%) and/or less than 5% of benzene.
  • the composition may preferably comprise 10-40% triptane, less than 5% benzene and have a Reid Vapour Pressure at 37.8°C measured according to ASTMD323 of 30-120kPa.
  • the composition is usually an unleaded motor gasoline base blend composition.
  • the present invention also provides an unleaded formulated motor gasoline which comprises said base composition and at least one motor gasoline additive.
  • R is hydrogen the hydrocarbon is triptane. If R is methyl the hydrocarbon is 2,2,3 trimethylpentane. Especially preferred is triptane. Triptane and 2,2,3 trimethylpentane may be used individually or in combination with each other, for example, in a weight ratio of 10:90 - 90:10, preferably, 30:70 - 70:30.
  • the hydrocarbon of formula I preferably triptane may be present in amount of 5-95% or 8-90% such as 10-90%, or 15-65% e.g. 10-40% such as 20-35% by volume or 40-90% such as 40-55% or 55-80% or 8-35% such as 8-20% by volume. Unless otherwise stated all percentages in this specification are by volume, and disclosures of a number of ranges of amounts in the composition or gasoline for 2 or more ingredients includes disclosures of all sub-combinations of all the ranges with all the ingredients.
  • Triptane or 2,2,3 trimethylpentane may be used in a purity of at least 95% but is preferably used as part of a hydrocarbon mixture e.g. with at least 50% of the compound of formula I.
  • This mixture may be obtained for example by alkylation of an iso alkane e.g. reaction of propene and iso butane or obtained via distillation of the product of a catalytic cracking reaction to give a C 4 fraction containing olefin and hydrocarbon, alkylation to produce a C 4-9 especially a C 6-9 fraction which is distilled to give a predominantly C 8 fraction, which usually contains trimethyl pentanes including 2,2,3 trimethyl pentane and/or 2,3,3 trimethyl pentane.
  • triptane this fraction can be demethylated to give a crude product comprising at least 5% of triptane, which can be distilled to increase the triptane content in the mixture; such a distillate may comprise at least 10% or 20% of triptane and 2,2,3 trimethylpentane but especially at least 50% e.g. 50-90% the rest being predominantly of other aliphatic C7 and C8 hydrocarbons e.g. in amount 10-50% by volume.
  • Triptane may be prepared generally as described in Rec. Trav. Chim. 1939, Vol.58 pp 347-348 by J.P.Wibaut et al, which involves reaction of pinacolone with methyl magnesium iodide followed by dehydration (e.g. with sulphuric acid) to form triptene, which is hydrogenated e.g. by catalytic hydrogenation to triptane.
  • triptane and 2,2,3 trimethylpentane may be used in any commercially available form.
  • the gasoline composition also contains as component (b) at least one liquid saturated hydrocarbon of 5-10 carbons especially predominantly branched chain C 7 or C 8 compounds e.g. iso C 7 or iso C 8 .
  • This hydrocarbon may be substantially pure e.g. n-heptane, isooctane or isopentane or a mixture e.g. a distillation product or a reaction product from a refinery reaction e.g. alkylate.
  • the hydrocarbon may have a Motor Octane Number (MON) of 0-60 but preferably has a MON value of 60-96 such as isomerate (bp 25-80°C).
  • Research Octane Number RON may be 80-105 e.g. 95-105, while the ROAD value (average of MON and RON) may be 60-100.
  • Component (b) may comprise a hydrocarbon component having boiling point (preferably a final boiling point) higher than, preferably one boiling at least 20°C more than, the compound of formula I e.g. triptane such as 20-60°C more than triptane but less than 225°C e.g. less than 170°C and usually is of Motor Octane Number of at least 92 e.g. 92-100; such components are usually alkanes of 7-10 carbons especially 7 or 8 carbons, and in particular have at least one branch in their alkyl chain, in particular 1-3 branches, and preferably on an internal carbon atom and especially contain at least one -C(CH 3 ) 2 - group.
  • the volume amount of the component (b) in total is usually 10-80% e.g. 25-70%, 40-65% or 20-40%, the higher percentages being usually used with lower percentages of component (a).
  • Component (b) may be a mixture of the liquid saturated hydrocarbons e.g. a distillation product e.g. naphtha or straight run gasoline or a reaction product from a refinery reaction e.g. alkylate including aviation alkylate (bp 30-190°C) isomerate (bp 25-80°C), light reformate (bp 20-79°C) or light hydrocrackate.
  • the mixture may contain at least 60% or at least 70% w/w e.g. 60-95 or 70-90% w/w liquid saturated aliphatic hydrocarbon.
  • Volume amounts in the composition of the invention of the component (b) mixtures (primarily saturated liquid aliphatic hydrocarbon fractions e.g.
  • the total of isomerate, alkylate, naphtha and straight run gasoline (in each case (if any) present in the composition) may be 4-60%, such as 4-25% or preferably 10-55% such as 25-45%.
  • Alkylate or straight run gasoline are preferably present, optionally together but preferably in the absence of the other, in particular in amount of 2-50% such as 10-45 e.g. 10-25%, 25-45% or 25-40%.
  • the compositions of the invention may also comprise naphtha e.g. in volume amount of 0-25% such as 2-25%,10-25% or 2-10%.
  • compositions may comprise a hydrocarbon component which is a saturated aliphatic hydrocarbon of 4-6 carbons and which is more volatile and has a lower boiling point (preferably a lower final boiling point) than the compound of Formula I in particular one boiling at least 30°C such as 30-60°C below that of triptane at atmospheric pressure, and especially is itself of Motor Octane Number greater than 88 in particular at least 90 e.g. 88-93 or 90-92.
  • the hydrocarbon component include alkanes of 4 or 5 carbons in particular iso-pentane, which may be substantially pure or crude hydrocarbon fraction from alkylate or isomerate containing at least 30% e.g.
  • the hydrocarbon component may be an alkane of boiling point (at atmospheric pressure) 60-100°C less than that of triptane e.g. n and/or iso butane optionally in blends with the C 5 alkane of 99.5:0.5 to 0.5:99.5, e.g. 88:12 to 75:25.
  • n Butane alone or mixed with isopentane is preferred, especially in the above proportions, and in particular with a volume amount of butane in the composition of up to 20% such as 1-15% e.g. 1-8, 3-8 or 8-15%.
  • Cycloaliphatic hydrocarbons e.g. of 5-7 carbons such as cyclopentane or cyclohexane may be present but usually in amounts of less than 15% of the total e.g. 1-10%.
  • Volume amounts in the composition of the total of isomerate, alkylate, naphtha, straight run gasoline, 4-6 carbon liquid aliphatic hydrocarbon (as defined above) and cycloaliphatic hydrocarbon (in each case if present) may be 5-60%, such as 8-25%, 15-55% such as 30-50%.
  • the gasoline compositions of the invention also preferably contain at least one olefin, (in particular with one double bond per molecule) which is a liquid alkene of 5-10 e.g. 6-8 carbons, such as a linear or branched alkene e.g. pentene, isopentene hexene, isohexene or heptene or 2 methyl 2 pentene, or a mixture comprising alkenes which may be made by cracking e.g. catalytically or thermally cracking a residue from crude oil, e.g. atmospheric or vacuum residue; the mixture may be heavy or light catalytically cracked spirit (or a mixture there of). The cracking may be steam assisted.
  • olefin (in particular with one double bond per molecule) which is a liquid alkene of 5-10 e.g. 6-8 carbons, such as a linear or branched alkene e.g. pentene, isopentene hexene, isohe
  • olefin containing mixtures are "C6 bisomer", catalytic polymerate, and dimate.
  • the olefinic mixtures usually contain at least 10% w/w olefins, such as at least 40% such as 40-80% w/w.
  • Preferred mixtures are (xi) steam cracked spirit (xii) catalytically cracked spirit (xiii) C6 bisomer and (xiv) catalytic polymerate, though the optionally cracked catalytically spirits are most advantageous.
  • Amounts in the total composition of the olefinic mixtures especially the sum of (xi) - (xiv) (if any present) maybe 0-55, e.g.
  • Amounts of (xi) and (xii) (if present) in total in the composition are preferably 18-55, such as 18-35, 18-30 or 35-55% (by volume).
  • the olefin or mixture of olefins usually has an MON value of 70-90, usually a RON value of 85-95 and a ROAD value of 80-92.
  • the volume amount of olefin(s) in total in the gasoline composition of the invention may be 0% or 0-30%, e.g. 0.1-30% such as 1-30% in particular 2-25, 5-30, (especially 3-10), 5-18.5, 5-18 or 10-20%.
  • the composition contains at least 1% olefin and a maximum of 18% or especially a maximum of 14%, but may be substantially free of olefin.
  • compositions may also contain at least one aromatic compound, preferably an alkyl aromatic compound such as toluene or o, m, or p xylene or a mixture thereof or a trimethyl benzene.
  • the aromatics may have been added as single compounds e.g. toluene, or may be added as an aromatics mixture containing at least 30% w/w aromatic compounds such as 30-100% especially 50-90%.
  • Such mixtures may be made from catalytically reformed or cracked gasoline obtained from heavy naphtha. Example of such mixtures are (xxi) catalytic reformate and (xxii) heavy reformate. Amounts of the single compounds e.g.
  • toluene in the composition may be 0-35%, such as 2-33% e.g. 10-33%, while amounts of the aromatics mixtures especially the total of the reformates (xxi) & (xxii) (if any) in the composition may be 0-50%, such as 1-33% e.g. 2-15% or 2-10% or 15-32% v/v, and total amount of reformates (xxi), (xxii) and added single compounds (e.g. toluene) may be 0-50% e.g. 0.5-20% or 5-40, such as 15-35 or 5-25% v/v.
  • the aromatics usually have a MON value of 90-110 e.g. 100-110 and a RON value of 100-120 such as 110-120 and a ROAD value of 95-110.
  • the volume amount of aromatic compounds in the composition is usually 0% or 0-50% such as less than 40% or less than 28% or less than 20% such as 1-50%, 2-40%, 3-28%, 4-25%, 5-20% (especially 10-20%), 4-10% or 20-35% especially of toluene.
  • the gasoline composition may also be substantially free of aromatic compound. Amounts of aromatic compounds of less than 42%, e.g. less than 35% or especially less than 30% are preferred.
  • the amount of benzene is less than 5% preferably less than 1.5% or 1% e.g. 0.1-1% of the total volume or less than 0.1% of the total weight of the composition.
  • compositions may also contain at least one oxygenate octane booster, usually an ether, usually of Motor Octane Number of at least 96-105 e.g. 98-103.
  • the ether octane booster is usually a dialkyl ether, in particular an asymmetric one, preferably wherein each alkyl has 1-6 carbons, in particular one alkyl being a branched chain alkyl of 3-6 carbons in particular a tertiary alkyl especially of 4-6 carbons such as tert-butyl or tert-amyl, and with the other alkyl being of 1-6 e.g. 1-3 carbons, especially linear, such as methyl or ethyl.
  • oxygenates examples include methyl tertiary butyl ether (MTBE), ethyl tertiary butyl ether and methyl tertiary amyl ether.
  • the oxygenate may also be an alcohol of 1-6 carbons e.g. ethanol.
  • the volume amount of the oxygenate may be 0 or 0-25% such as 1-25%, 2-20% , 2-10% or 5-20% especially 5-15%, but advantageously less than 3% such as 1-3% (especially of MTBE and/or ethanol).
  • the oxygenate may also be substantially absent from the composition or gasoline of the invention.
  • Aromatic amines e.g. liquid ones such as aniline may be present if at all in amount of less than 5% by volume, and are preferably substantially absent e.g. less than 100ppm.
  • the relative volume ratio of the amine to triptane is usually less than 3:1 e.g. less than 1:2.
  • the composition of the invention contains components (a) and (b), and the formulated unleaded gasoline also contains at least one motor gasoline additive, for example as listed in ASTM D-4814 the contents of which is herein incorporated by reference or specified by a regulatory body, e.g. US California Air Resources Board (CARB) or Environmental Protection Agency (EPA).
  • CARB California Air Resources Board
  • EPA Environmental Protection Agency
  • These additives are distinct from the liquid fuel ingredients, such as MTBE.
  • Such additives may be the lead free ones described in Gasoline and Diesel Fuel Additives, K Owen, Publ. By J.Wiley, Chichester, UK, 1989, Chapters 1 and 2, USP 3955938, EP 0233250 or EP 288296, the contents of which are herein incorporated by reference.
  • the additives maybe pre-combustion or combustion additives.
  • additives are anti-oxidants, such as one of the amino or phenolic type, corrosion inhibitors, anti-icing additives e.g. glycol ethers or alcohols, engine detergent additives such as ones of the succinic acid imide, polyalkylene amine or polyether amine type and anti-static additives such as ampholytic surface active agents, metal deactivators, such as one of thioamide type, surface ignition inhibitors such as organic phosphorus compounds, combustion improvers such as alkali metal salts and alkaline earth metal salts of organic acids or sulphuric acid monoesters of higher alcohols, anti valve seat recession and additives such as alkali metal compounds, e.g.
  • anti-oxidants such as one of the amino or phenolic type
  • corrosion inhibitors such as one of the amino or phenolic type
  • anti-icing additives e.g. glycol ethers or alcohols
  • engine detergent additives such as ones of the succinic acid imide, polyalkylene amine or polyether
  • additives such as borates or carboxylates and colouring agents, such as azodyes.
  • One or more additives e.g. 2-4 of the same or different types may be used, especially combinations of at least one antioxidant and at least one detergent additive.
  • Antioxidants such as one or more hindered phenols e.g. ones with a tertiary butyl group in one or both ortho positions to the phenolic hydroxyl group are preferred in particular as described in Ex. 1 hereafter.
  • the additives may be present in the composition in amounts of 0.1-100ppm e.g. 1-20ppm of each, usually of an antioxidant especially one or more hindered phenols. Total amounts of additive are usually not more than 1000ppm e.g. 1-1000ppm.
  • compositions and gasolines are free of organolead compounds, and usually of manganese additives such as manganese carbonyls.
  • compositions and gasolines may contain up to 0.1% sulphur, e.g. 0.000-0.02% such as 0.002-0.01%w/w.
  • the gasoline compositions of the invention usually have a MON value of at least 80 e.g. 80-110 or 80-105 such as 98-105 or preferably 80 to less than 98, such as 80-95, 83-93 or 93-98.
  • the RON value is usually 90-120 e.g. 102-120 or preferably 90-102 preferably 90-100 e.g. 90-99, such as 90-93 e.g. 91, or 93-98 e.g. 94.5-97.5, or 97-101 while the ROAD value 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 MON 80-83, RON 90-93, and ROAD 85-90, or MON 83-93, RON 93-98 and ROAD 85-95 or MON 83-93, RON 97-101 and ROAD 90-95.
  • the Net calorific value of the gasoline (also called the Specific Energy) is usually at least 18000 Btu/lb e.g. at least 18500, 18700 or 18,900 such as 18500-19500, such as 18700-19300 or 18900-19200; the calorific value may be at least 42MJ/kg e.g. at least 43.5 MJ/kg such as 42-45 or 43-45 such as 43.5-44.5MJ/kg.
  • the gasoline usually has a boiling range (ASTM D86) of 20-225°C, in particular with at least 2% e.g. 2-15% boiling in the range 171-225°C.
  • the gasoline is usually such that at 70°C at least 10% is evaporated while 50% is evaporated on reaching a temperature in the range 77-120°C preferably 77-116°C and by 185°C, a minimum of 90% is evaporated.
  • the gasoline is also usually that 10-50% may be evaporated at 70°C, 40-74% at 100°C, 70-97% at 150°C and 90-99% may be evaporated at 180°C.
  • the Reid Vapour Pressure of the gasoline at 37.8°C measured according to ASTM D323 is usually 30-120, e.g. 40-100 such as 61-80 or preferably 50-80, 40-65, e.g. 40-60 or 40-50Kpa.
  • the gasoline compositions when free of any oxygenates usually have a H:C atom ratio of at least 1.8:1 e.g. at least 2.0:1 or at least 2.1 or 2.2:1, such as 1.8-2.3:1 or 2.0-2.2:1.
  • the gasoline composition meets the following criteria.
  • Atom H:C x [1 + oxy] x [ Net Heat of Combustion 200 + ROAD] ⁇ y wherein Atom H:C is the fraction of hydrogen to carbon in the hydrocarbons in the composition, oxy means the molar fraction of oxygenate, if any in the composition, Net Heat of Combustion is the energy derived from burning 1lb (454g) weight of fuel (in gaseous form) in oxygen to give gaseous water and carbon dioxide expressed in Btu/lb units [MJ/kg times 430.35], and y is at least 350, 380, 410 or 430, in particular 350-440 e.g. 380-420 especially 400-420.
  • the motor gasoline of this invention comprises 10-90% of triptane, 10-80% of component (b), 0-25% naphtha, 0-15% of butane, 5-20% of olefin, 3-28% aromatics and 0-25% oxygenate, in particular with 5-20% aromatics and 5-15% olefins.
  • the motor gasoline of this invention contains 8-65% of triptane (especially 15-35%), 0.1-30% such as 2-25% olefins, especially 3-14% and 0-35% aromatics such as 0-30% e.g. 5-35, 5-20 (especially 5-15%) or 20-30%, and 5-50% component (b) mixtures e.g. 10-45% such as 20-40%.
  • Such gasolines may also contain oxygenates, such as MTBE especially in amount of less than 3% e.g. 0.1-3% and especially contain less than 1.5% benzene e.g. 0.1-1%.
  • Such gasolines preferably have RON of 97-99, MON 87-90 and ROAD values of 92-94.5.
  • Examples of motor gasolines of the invention are ones with 5-25% triptane, 5-15% olefins, 15-35% aromatics and 40-65% component (b), in particular 15-25% triptane, 7-15%, olefins 15-25% aromatics and 45-52% component (b) mixture of RON value 96.5-97.5, or 5-15% triptane, 7-15% olefins, 15-25% aromatics and 55-65% compound (b) of RON value 94.5-95.5.
  • Examples of motor gasolines of the invention are ones having 1-15% e.g. 3-12% butane, 0-20% e.g. 5-15% ether e.g. MTBE, 20-80 e.g. 25-70% of refinery mixed liquid (usually C 6 -C 9 )streams (apart from naphtha) (such as mixtures of (i)-(iv) above), 0-25% e.g. 2-25% naphtha, 5-70% e.g. 15-65% triptane, with RON 93-100 e.g. 94-98, MON 80-98 e.g. 83-93 or 93-98, and RVP 40-80 such as 40-65Kpa.
  • refinery mixed liquid usually C 6 -C 9
  • naphtha such as mixtures of (i)-(iv) above
  • RON 93-100 e.g. 94-98
  • MON 80-98 e.g. 83-93 or
  • Such gasolines usually contain 1-30% e.g. 2-25% olefins and 2-30% e.g. 4-25% aromatics. Amounts of olefins of 15-25% are preferred for RON values of 94-98 e.g. 94-96 and 2-15% e.g. 2-7% for RON values of 96-100 such as 96-98.
  • fuel compositions of the invention contain 8-18% triptane, 10-50% e.g. 25-40% of total component (b) mixture, 5-40% e.g. 20-35% of total aromatics mixture 15-60, e.g. 15-30% or 40-60% of total olefinic mixture and 0-15% total oxygenate e.g. 3-8% or 8-15%.
  • Especially preferred compositions have 8-18% triptane, 25-40% total mixed component (b) mixture, 20-35% total aromatics, and 15-30% total olefinics, or 8-18% triptane, 15-40% total mixed component (b) mixture, 3-25% total aromatics mixture, and 40-60% total olefinic mixture.
  • fuel compositions contain 20-40% triptane, 8-55% of the total component (b) mixture, e.g. 5-25% or 35-55%, and 0 or 5-25% e.g. 18-25% total aromatics mixture, 0-55 especially 10-55 or 40-55% total olefin mixture, especially preferred compositions having 20-40% triptane, 5-25% total component (b) mixtures, 3-25% total aromatics mixture and 40-60% total olefinic mixture, or 20-40% triptane, 35-55% total component (b) mixture 15-30% total aromatics mixture and 0-15% e.g.
  • total olefin mixture or in particular 20-40% triptane, 25-45% or 30-50% total component (b) mixture, 2-15% total aromatics mixture 18-35% total olefins mixture, and especially 3-10% or 5-18% olefins, and 10-35% such as 10-20% aromatics (e.g. 10-18%).
  • Example of fuel compositions contain 30-55% e.g. 40-55% triptane, 5-30% total component (b) mixture 0-10% total aromatic mixture, 10-45% olefinic mixture and 0-15% oxygenates especially with the total of oxygenates and olefinic mixture of 20-45%.
  • Other examples of fuel compositions contain 55-70% triptane, 10-45% total component b, e.g. 10-25% or 35-45%, and 0-10% e.g. 0 or 0.5-5% total aromatics Mixture, and 0-30% total olefinics mixtures, e.g. 0 or 15-30%, especially 55-70% triptane 10-25% total component (b) 0 or 0.5-5% total aromatics mixture and 15-30% total olefinic mixture.
  • fuel composition comprise 15-35% e.g. 20-35% triptane, 0-18.5% e.g. 2-18.5% olefin, 5-40% e.g. 5-35% aromatics 25-65% saturates and less than 1% benzene, and 18-65% e.g 40-65% triptane, 0-18-5% e.g. 5-18.5% olefins, 5-42% e.g. 5-28% aromatics, 35-55% saturates and less than 1% benzene.
  • Another fuel composition may comprise 25-40% e.g. 30-40% such as 35% of alkylate, 10-25% e.g. 15-25% such as 20% of isomerate, 10-25% e.g. 15-25% such as 20% of light hydrocrackate and 20-35% e.g. 20-30% such as 25% of triptane and optionally 0-5% butane.
  • Such a composition is preferably substantially paraffinic and is substantially free of olefins and aromatics.
  • Antiknock Index also known as The ROAD Index
  • MON the average of MON and RON.
  • compositions may comprise 8-30% triptane e.g. 15-30%, and 10-50% e.g. 20-40% total component (b) mixture, 5-30%, e.g. 5-20% total olefins and 10-40 e.g. 15-35% total aromatics, or 8-30% triptane, 10-50% total component (b) mixture, 5-40% total aromatic mixtures e.g. 20-30% and 10-60% e.g. 30-55% total olefinic mixtures.
  • compositions may comprise 5-25% (or 5-15%) triptane, 20-45% total component (b) mixture, 0-25% e.g. 1-10 or 10-25% total olefins, and 10-35% e.g. 10-20% or 20-35% total aromatics or 5-25% (5-15%) triptane, 20-45% total component (b) mixture, 0-35% total aromatic mixtures e.g. 1-15 or 15-35%, and 5-65% e.g. 5-30 or 30-65% total olefinic mixtures.
  • the fuel compositions of the invention may comprise 5-65% e.g. 5-20, 20-30, 30-65 or 40-65% triptane and 5-40% (5-35%) e.g. 5-12 or 12-40% (12-30%) total component (b) mixture 1-30% e.g. 1-10 or 10-25% total olefins and 5-55% e.g. 5-15 or 15-35 or 35-55% total aromatics, or the above amounts of triptane with 0-55 e.g. 0.5-25% e.g. 10-25% or 25-55% of aromatic fractions and 0 or 10-60% e.g. 10-30% or 35-60% total olefin fractions.
  • the fuel compositions may comprise 20-65% triptane e.g. 40-65% triptane, 0-15% e.g. 5-15% total olefins, 0-20% e.g. 5-20% total aromatics and 5-50 e.g. 30-50% total component (b) mixture, or the above amounts of triptane and total component (b) mixture with 0-30% e.g. 10-30% aromatic fractions and 0-30 e.g. 5-30% olefinic fraction, or the above amounts of triptane e.g. 20-40% triptane, total component b mixture, total olefins and total aromatics, with 2-15% aromatic fractions and 18-35% olefinic fractions.
  • the invention can provide motor gasolines, in particular of 91, 95, 97, 98 and 110 RON values, with desired high Octane Levels but low emission values on combustion in particular of at least one of total hydrocarbons, total air toxics, NOx, carbon monoxide, and carbon dioxide, especially of both total hydrocarbons and NOx.
  • the invention also provides the use of a compound of formula I, in particular triptane, in unleaded motor gasoline of MON at least 80 e.g. 80 to less than 98, e.g. as an additive to or component therein, to reduce the emission levels on combustion, especially of at least one of total hydrocarbons, total air toxics NOx, carbon monoxide and carbon dioxide especially both of total hydrocarbons and NOx.
  • the invention also provides a method of reducing emissions of exhaust gases in the combustion of unleaded motor gasoline fuels of MON of at least 80 which comprises having a compound of formula I present in the fuel which is a gasoline of the invention.
  • the invention also provides use of an unleaded gasoline of the invention in a spark ignition combustion engine to reduce emissions of exhaust gases. While the compositions of the invention may be used in supercharged or turbocharged engines, they are preferably not so used, but are used in normally aspirated ones.
  • the compound of formula I e.g. triptane can reduce one or more of the above emission levels better than amounts of alkylate or a mixture of aromatics and oxygenate at similar Octane Number and usually decrease the fuel consumption as well.
  • Formulated gasolines were made by mixing each blend with a phenolic antioxidant 55% minimum 2,4 dimethyl-6-tertiary butyl phenol 15% minimum 4 methyl-2, 6-ditertiary-butyl phenol with the remainder as a mixture of monomethyl and dimethyl-tertiary butyl phenols.
  • mixed fractions means a blend of refinery fractions in which HCC is heavy catalytically cracked spirit, LCC is light catalytically cracked spirit and SRG is straight run gasoline.
  • the fuels were tested in a single cylinder research engine at a number of different engine settings.
  • the speed/load was 20/7.2 rps/Nm/, or 50/14.3 rps/Nm the LAMBDA setting was 1.01 or 0.95, and the ignition setting was set or optimized.
  • the emissions of CO, CO 2 , total hydrocarbons, NOx, and total air toxics (benzene, butadiene, formaldehyde and acetaldehyde) were measured from the exhaust gases.
  • the results from the different engine settings were averaged and showed that, compared to the base blend (Comp. Ex. A) the emissions with the compositions containing heavy reformate and MTBE (Comp. C), 25% alkylate (Comp.
  • Example % CO %CO 2 %THC %NOx %TAT %FC Comp C (MTBE -4.9 -2.3 -6.2 -6.5 -9.2 +1.4 Comp B (alkylate) -7.9 -4.5 -4.0 -8.0 -13.1 -2.9 8 /triptane -9.6 -5.6 -6.6 -10.1 -18.7 -4.1
  • THC total hydrocarbons
  • TAT total air toxics.
  • FC Fuel Consumption
  • Emission characteristics were obtained as in Ex.8 (apart from Lamba settings of 1.00 and 0.95 set for the base fuel (Comp.D) on combustion of a series of gasoline fuels with different components namely reformate, (high aromatics), (Comp.D), triptane, Ex.24-27 and triptane/ethanol Ex.28. Fuel consumption was also measured in g/kWhr.
  • Formulated gasolines were made by addition of the phenolic antioxidant in amount and nature as in Ex.1-7. The compositions were as shown in Table 3. The results were expressed in Table 4 as the percentage change in emissions or in fuel consumption compared to Ex.D.
  • Example 24 25 26 27 28 D Composition % v/v Triptane 40 10 25 60 10 Butane 2.96 2.96 2.96 2.96 2.96 Mixed Fractions (apart from 87.04 72.04 37.04 Naphtha) of which Catalytic reformate 19.78 4.78 21.28 25.25 CCS 5 5 5 5 10 5 Steam cracked spirit 37.2 47.42 47.42 17.2 9.7 47.42 SRG 15.72 Toluene 4.53 Naphtha 13.79 Ethanol 5 Heavy reformate 9.51 Cyclohexane 5 5 5 5 5 5 5 5 5 Light hydrocrackate 7.93 7.93 7.93 7.93 C6 Bisomer 1.91 1.91 1.91 1.91 Analysis, %v/v Aromatics 15.0 31.2 21.7 7.8 31.1 39.2 Olefins 13.4 16.2 16.1 8.3 6.5 16.2 Sulphur % w/w 0.007 0.007 0.007 0.012 0.007 Antioxidant mg/l 10 10 10 10 10 10 Distillation
  • gasoline fuels (Ex.29, F and G) were compared for production of emissions on combustion in cars.
  • the gasoline fuels had the compositions and properties as shown in Table 5 and the formulated gasolines included antioxidant as in Ex.1.
  • the fuels met the requirements of 2005 Clean Fuel specification according to Directive 98/70 EC Annexe 3.
  • the cars were regular production models, namely 1998 Ford Focus (1800cc), 1996-7 VW Golf (1600cc), 1998 Vauxhall Corsa (1000cc), 1994-5 Peugeot 106 (1400cc) and 1998 Mitsubishi GDI (1800cc) each fitted with a catalytic converter.
  • the Corsa had 3 cylinders, the rest 4 cylinders, while the 106 had single point injection; the Mitsubishi had direct injection and the rest multipoint injection for their combustion.
  • the CO 2 emissions averaged over the 5 cars were lower with the triptane fuel (Ex.29) compared to the averaged base fuel results (Comp.F, G), namely Total tailpipe emissions in EDC tests, EUDC test and ECE test, the reductions being respectively 2.8%, 2.7% and 2.8%.
  • the Fuel Consumptions averaged over the 5 cars were lower with the triptane fuel (Ex.29) compared to the averaged base results (Comp.F, G) in those same tests, the reductions being respectively, 0.6%, 0.6% and 0.5%.
  • the tailpipe emissions results for THC, CO and NO x in at least some parts of the total EDC cycle showed trends towards triptane giving lower emissions than the base fuel, but the differences may or may not be confirmed in view of the limited number of vehicles tested.
  • the ECE tests simulates city driving and has 4 identical repeats of a specified speed profile, which profile has 3 progressively higher speed sections interspersed by zero speed sections (the average speed being 19km/hr).
  • the first profile corresponds to driving from a cold start.
  • a cold engine the effects of friction, lubricants and the nature of the fuel among others, differ from those with a hot engine in an unpredictable way, and it is with cold engines that most tailpipe emissions are produced, because the catalytic converter becomes increasingly effective at reducing emissions when it becomes hot.
  • Lambda sensor upstream of the converter controls the fuel/air ratio entering the engine, but this is not effective with a cold engine (resulting in an unregulated fuel/air ratio); after cold start the sensor quickly becomes effective, (resulting in a regulated fuel/air ratio), even when the catalyst is not yet hot enough to be effective.
  • cold start operations are different from hot running operations and yet contribute to a large amount of tailpipe emissions.
  • This period of cold start simulated as above may correspond in real life to a period of time or distance, which may vary, depending on how the car is driven and/or ambient conditions e.g. up to 1 km or 4 or 2 min, or a temperature of the engine coolant (e.g. radiator water temperature) of up to 50°C.
  • the car engine may also be deemed cold if it has not been operated for the previous 4hr before start, usually at least 6hr before start.
  • the present invention also provides of method of reducing emissions of exhaust gases in the combustion of unleaded gasoline fuels of MON of at least 80 e.g. 80 to less than 98 from cold start of a spark ignition combustion engine, which comprises having a compound of formula I present in the fuel which is a gasoline of the invention.

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Abstract

An unleaded formulated motor gasoline comprising a base blend composition having a MON of at least 80 e.g. 80 to less than 98 comprises component (a) at least 5% (by volume of the total composition) of at least one hydrocarbon having the following formula I R-CH2-CH(CH3)-C(CH3)2-CH3 wherein R is hydrogen or methyl, especially triptane, and component (b) at least one saturated liquid aliphatic hydrocarbon having 4 to 12 carbon atoms.
The corresponding unleaded formulated motor gasoline comprises also at least one motor gasoline additive.
The blend or gasoline preferably contains at least one of aromatics, olefins, and oxygenates. The gasolines or blends give rise on combustion to reduced levels of emissions of exhaust gases, in particular carbon dioxide, carbon monoxide, nitrogen oxides and total hydrocarbons.

Description

  • This invention relates to a fuel composition, in particular a gasoline composition for use in motor vehicles.
  • For many years manufacturers of spark ignition combustion engines have been striving for higher efficiency to make optimum use of the hydrocarbon fuels. But such engines require gasolines of higher octane number, which has been achieved in particular by addition of organo lead additives, and latterly with the advent of unleaded gasolines, by addition of MTBE. But combustion of any gasoline gives rise to emissions in the exhaust gases, e.g. of carbon dioxide, carbon monoxide, nitrogen oxides (NOx) and toxic hydrocarbons and such emissions are undesirable.
  • Motor gasolines have been discovered having high Octane Number but producing low emissions on combustion.
  • The present invention provides an unleaded blend composition having a Motor Octane Number (MON) of at least 80 comprising component (a) at least 5% or preferably at least 8 or 10% (by volume of the total composition) of at least one hydrocarbon having the following formula I R-CH2-CH(CH3)-C(CH3)2-CH3 wherein R is hydrogen or methyl
    and component (b) at least one saturated liquid aliphatic hydrocarbon having 4 to 12, 4-10 such as 5-10 e.g. 5 - 8 carbon atoms. In another embodiment component (b) is contained in at least one of isomerate, alkylate, straight run gasoline, light reformate, light hydrocrackate and aviation alkylate. Preferably the composition comprises at least one of an olefin (e.g. in amount of 1-30%) and/or at least one aromatic hydrocarbon (e.g. in amount of 1-50%, especially 3-28%) and/or less than 5% of benzene. The composition may preferably comprise 10-40% triptane, less than 5% benzene and have a Reid Vapour Pressure at 37.8°C measured according to ASTMD323 of 30-120kPa. The composition is usually an unleaded motor gasoline base blend composition.
  • The present invention also provides an unleaded formulated motor gasoline which comprises said base composition and at least one motor gasoline additive.
  • If R is hydrogen the hydrocarbon is triptane. If R is methyl the hydrocarbon is 2,2,3 trimethylpentane. Especially preferred is triptane. Triptane and 2,2,3 trimethylpentane may be used individually or in combination with each other, for example, in a weight ratio of 10:90 - 90:10, preferably, 30:70 - 70:30.
  • The hydrocarbon of formula I, preferably triptane may be present in amount of 5-95% or 8-90% such as 10-90%, or 15-65% e.g. 10-40% such as 20-35% by volume or 40-90% such as 40-55% or 55-80% or 8-35% such as 8-20% by volume. Unless otherwise stated all percentages in this specification are by volume, and disclosures of a number of ranges of amounts in the composition or gasoline for 2 or more ingredients includes disclosures of all sub-combinations of all the ranges with all the ingredients.
  • Triptane or 2,2,3 trimethylpentane may be used in a purity of at least 95% but is preferably used as part of a hydrocarbon mixture e.g. with at least 50% of the compound of formula I. This mixture may be obtained for example by alkylation of an iso alkane e.g. reaction of propene and iso butane or obtained via distillation of the product of a catalytic cracking reaction to give a C4 fraction containing olefin and hydrocarbon, alkylation to produce a C4-9 especially a C6-9 fraction which is distilled to give a predominantly C8 fraction, which usually contains trimethyl pentanes including 2,2,3 trimethyl pentane and/or 2,3,3 trimethyl pentane. To produce triptane this fraction can be demethylated to give a crude product comprising at least 5% of triptane, which can be distilled to increase the triptane content in the mixture; such a distillate may comprise at least 10% or 20% of triptane and 2,2,3 trimethylpentane but especially at least 50% e.g. 50-90% the rest being predominantly of other aliphatic C7 and C8 hydrocarbons e.g. in amount 10-50% by volume. Triptane may be prepared generally as described in Rec. Trav. Chim. 1939, Vol.58 pp 347-348 by J.P.Wibaut et al, which involves reaction of pinacolone with methyl magnesium iodide followed by dehydration (e.g. with sulphuric acid) to form triptene, which is hydrogenated e.g. by catalytic hydrogenation to triptane. Alternatively triptane and 2,2,3 trimethylpentane may be used in any commercially available form.
  • The invention will be further described with triptane exemplifying the compound of formula I but 2,2,3 trimethylpentane may be used instead or as well.
  • The gasoline composition also contains as component (b) at least one liquid saturated hydrocarbon of 5-10 carbons especially predominantly branched chain C7 or C8 compounds e.g. iso C7 or iso C8. This hydrocarbon may be substantially pure e.g. n-heptane, isooctane or isopentane or a mixture e.g. a distillation product or a reaction product from a refinery reaction e.g. alkylate. The hydrocarbon may have a Motor Octane Number (MON) of 0-60 but preferably has a MON value of 60-96 such as isomerate (bp 25-80°C). Research Octane Number RON may be 80-105 e.g. 95-105, while the ROAD value (average of MON and RON) may be 60-100.
  • Component (b) may comprise a hydrocarbon component having boiling point (preferably a final boiling point) higher than, preferably one boiling at least 20°C more than, the compound of formula I e.g. triptane such as 20-60°C more than triptane but less than 225°C e.g. less than 170°C and usually is of Motor Octane Number of at least 92 e.g. 92-100; such components are usually alkanes of 7-10 carbons especially 7 or 8 carbons, and in particular have at least one branch in their alkyl chain, in particular 1-3 branches, and preferably on an internal carbon atom and especially contain at least one -C(CH3)2- group.
  • The volume amount of the component (b) in total (or the volume amount of mixtures comprising component (b), such as the total of each of the following (if present) (i)-(iv)) (i) catalytic reformate, (ii) heavy catalytic cracked spirit, (iii) light catalytic cracked spirit and (iv) straight run gasoline in the composition is usually 10-80% e.g. 25-70%, 40-65% or 20-40%, the higher percentages being usually used with lower percentages of component (a).
  • Component (b) may be a mixture of the liquid saturated hydrocarbons e.g. a distillation product e.g. naphtha or straight run gasoline or a reaction product from a refinery reaction e.g. alkylate including aviation alkylate (bp 30-190°C) isomerate (bp 25-80°C), light reformate (bp 20-79°C) or light hydrocrackate. The mixture may contain at least 60% or at least 70% w/w e.g. 60-95 or 70-90% w/w liquid saturated aliphatic hydrocarbon.
    Volume amounts in the composition of the invention of the component (b) mixtures (primarily saturated liquid aliphatic hydrocarbon fractions e.g. the total of isomerate, alkylate, naphtha and straight run gasoline (in each case (if any) present in the composition) may be 4-60%, such as 4-25% or preferably 10-55% such as 25-45%. Alkylate or straight run gasoline are preferably present, optionally together but preferably in the absence of the other, in particular in amount of 2-50% such as 10-45 e.g. 10-25%, 25-45% or 25-40%. The compositions of the invention may also comprise naphtha e.g. in volume amount of 0-25% such as 2-25%,10-25% or 2-10%.
  • The compositions may comprise a hydrocarbon component which is a saturated aliphatic hydrocarbon of 4-6 carbons and which is more volatile and has a lower boiling point (preferably a lower final boiling point) than the compound of Formula I in particular one boiling at least 30°C such as 30-60°C below that of triptane at atmospheric pressure, and especially is itself of Motor Octane Number greater than 88 in particular at least 90 e.g. 88-93 or 90-92. Examples of the hydrocarbon component include alkanes of 4 or 5 carbons in particular iso-pentane, which may be substantially pure or crude hydrocarbon fraction from alkylate or isomerate containing at least 30% e.g. 30-80% such as 50-70%, the main contaminant being up to 40% mono methyl pentanes and up to 50% dimethyl butanes. The hydrocarbon component may be an alkane of boiling point (at atmospheric pressure) 60-100°C less than that of triptane e.g. n and/or iso butane optionally in blends with the C5 alkane of 99.5:0.5 to 0.5:99.5, e.g. 88:12 to 75:25. n Butane alone or mixed with isopentane is preferred, especially in the above proportions, and in particular with a volume amount of butane in the composition of up to 20% such as 1-15% e.g. 1-8, 3-8 or 8-15%.
  • Cycloaliphatic hydrocarbons e.g. of 5-7 carbons such as cyclopentane or cyclohexane may be present but usually in amounts of less than 15% of the total e.g. 1-10%.
  • Volume amounts in the composition of the total of isomerate, alkylate, naphtha, straight run gasoline, 4-6 carbon liquid aliphatic hydrocarbon (as defined above) and cycloaliphatic hydrocarbon (in each case if present) may be 5-60%, such as 8-25%, 15-55% such as 30-50%.
  • The gasoline compositions of the invention also preferably contain at least one olefin, (in particular with one double bond per molecule) which is a liquid alkene of 5-10 e.g. 6-8 carbons, such as a linear or branched alkene e.g. pentene, isopentene hexene, isohexene or heptene or 2 methyl 2 pentene, or a mixture comprising alkenes which may be made by cracking e.g. catalytically or thermally cracking a residue from crude oil, e.g. atmospheric or vacuum residue; the mixture may be heavy or light catalytically cracked spirit (or a mixture there of). The cracking may be steam assisted. Other examples of olefin containing mixtures are "C6 bisomer", catalytic polymerate, and dimate. The olefinic mixtures usually contain at least 10% w/w olefins, such as at least 40% such as 40-80% w/w. Preferred mixtures are (xi) steam cracked spirit (xii) catalytically cracked spirit (xiii) C6 bisomer and (xiv) catalytic polymerate, though the optionally cracked catalytically spirits are most advantageous. Amounts in the total composition of the olefinic mixtures especially the sum of (xi) - (xiv) (if any present) maybe 0-55, e.g. 10-55 or 18-37 such as 23-35 or 20-55 such as 40-55% Amounts of (xi) and (xii) (if present) in total in the composition are preferably 18-55, such as 18-35, 18-30 or 35-55% (by volume).
  • The olefin or mixture of olefins usually has an MON value of 70-90, usually a RON value of 85-95 and a ROAD value of 80-92.
  • The volume amount of olefin(s) in total in the gasoline composition of the invention may be 0% or 0-30%, e.g. 0.1-30% such as 1-30% in particular 2-25, 5-30, (especially 3-10), 5-18.5, 5-18 or 10-20%. Preferably the composition contains at least 1% olefin and a maximum of 18% or especially a maximum of 14%, but may be substantially free of olefin.
  • The compositions may also contain at least one aromatic compound, preferably an alkyl aromatic compound such as toluene or o, m, or p xylene or a mixture thereof or a trimethyl benzene. The aromatics may have been added as single compounds e.g. toluene, or may be added as an aromatics mixture containing at least 30% w/w aromatic compounds such as 30-100% especially 50-90%. Such mixtures may be made from catalytically reformed or cracked gasoline obtained from heavy naphtha. Example of such mixtures are (xxi) catalytic reformate and (xxii) heavy reformate. Amounts of the single compounds e.g. toluene in the composition may be 0-35%, such as 2-33% e.g. 10-33%, while amounts of the aromatics mixtures especially the total of the reformates (xxi) & (xxii) (if any) in the composition may be 0-50%, such as 1-33% e.g. 2-15% or 2-10% or 15-32% v/v, and total amount of reformates (xxi), (xxii) and added single compounds (e.g. toluene) may be 0-50% e.g. 0.5-20% or 5-40, such as 15-35 or 5-25% v/v.
  • The aromatics usually have a MON value of 90-110 e.g. 100-110 and a RON value of 100-120 such as 110-120 and a ROAD value of 95-110. The volume amount of aromatic compounds in the composition is usually 0% or 0-50% such as less than 40% or less than 28% or less than 20% such as 1-50%, 2-40%, 3-28%, 4-25%, 5-20% (especially 10-20%), 4-10% or 20-35% especially of toluene. The gasoline composition may also be substantially free of aromatic compound. Amounts of aromatic compounds of less than 42%, e.g. less than 35% or especially less than 30% are preferred. Preferably the amount of benzene is less than 5% preferably less than 1.5% or 1% e.g. 0.1-1% of the total volume or less than 0.1% of the total weight of the composition.
  • The compositions may also contain at least one oxygenate octane booster, usually an ether, usually of Motor Octane Number of at least 96-105 e.g. 98-103. The ether octane booster is usually a dialkyl ether, in particular an asymmetric one, preferably wherein each alkyl has 1-6 carbons, in particular one alkyl being a branched chain alkyl of 3-6 carbons in particular a tertiary alkyl especially of 4-6 carbons such as tert-butyl or tert-amyl, and with the other alkyl being of 1-6 e.g. 1-3 carbons, especially linear, such as methyl or ethyl. Examples of such oxygenates include methyl tertiary butyl ether (MTBE), ethyl tertiary butyl ether and methyl tertiary amyl ether. The oxygenate may also be an alcohol of 1-6 carbons e.g. ethanol.
  • The volume amount of the oxygenate may be 0 or 0-25% such as 1-25%, 2-20% , 2-10% or 5-20% especially 5-15%, but advantageously less than 3% such as 1-3% (especially of MTBE and/or ethanol). The oxygenate may also be substantially absent from the composition or gasoline of the invention.
  • Aromatic amines e.g. liquid ones such as aniline may be present if at all in amount of less than 5% by volume, and are preferably substantially absent e.g. less than 100ppm. The relative volume ratio of the amine to triptane is usually less than 3:1 e.g. less than 1:2.
  • The composition of the invention contains components (a) and (b), and the formulated unleaded gasoline also contains at least one motor gasoline additive, for example as listed in ASTM D-4814 the contents of which is herein incorporated by reference or specified by a regulatory body, e.g. US California Air Resources Board (CARB) or Environmental Protection Agency (EPA). These additives are distinct from the liquid fuel ingredients, such as MTBE. Such additives may be the lead free ones described in Gasoline and Diesel Fuel Additives, K Owen, Publ. By J.Wiley, Chichester, UK, 1989, Chapters 1 and 2, USP 3955938, EP 0233250 or EP 288296, the contents of which are herein incorporated by reference. The additives maybe pre-combustion or combustion additives. Examples of additives are anti-oxidants, such as one of the amino or phenolic type, corrosion inhibitors, anti-icing additives e.g. glycol ethers or alcohols, engine detergent additives such as ones of the succinic acid imide, polyalkylene amine or polyether amine type and anti-static additives such as ampholytic surface active agents, metal deactivators, such as one of thioamide type, surface ignition inhibitors such as organic phosphorus compounds, combustion improvers such as alkali metal salts and alkaline earth metal salts of organic acids or sulphuric acid monoesters of higher alcohols, anti valve seat recession and additives such as alkali metal compounds, e.g. sodium or potassium salts such as borates or carboxylates and colouring agents, such as azodyes. One or more additives (e.g. 2-4) of the same or different types may be used, especially combinations of at least one antioxidant and at least one detergent additive. Antioxidants such as one or more hindered phenols e.g. ones with a tertiary butyl group in one or both ortho positions to the phenolic hydroxyl group are preferred in particular as described in Ex. 1 hereafter. In particular the additives may be present in the composition in amounts of 0.1-100ppm e.g. 1-20ppm of each, usually of an antioxidant especially one or more hindered phenols. Total amounts of additive are usually not more than 1000ppm e.g. 1-1000ppm.
  • The compositions and gasolines are free of organolead compounds, and usually of manganese additives such as manganese carbonyls.
  • The compositions and gasolines may contain up to 0.1% sulphur, e.g. 0.000-0.02% such as 0.002-0.01%w/w.
  • The gasoline compositions of the invention usually have a MON value of at least 80 e.g. 80-110 or 80-105 such as 98-105 or preferably 80 to less than 98, such as 80-95, 83-93 or 93-98. The RON value is usually 90-120 e.g. 102-120 or preferably 90-102 preferably 90-100 e.g. 90-99, such as 90-93 e.g. 91, or 93-98 e.g. 94.5-97.5, or 97-101 while the ROAD value 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 MON 80-83, RON 90-93, and ROAD 85-90, or MON 83-93, RON 93-98 and ROAD 85-95 or MON 83-93, RON 97-101 and ROAD 90-95. The Net calorific value of the gasoline (also called the Specific Energy) is usually at least 18000 Btu/lb e.g. at least 18500, 18700 or 18,900 such as 18500-19500, such as 18700-19300 or 18900-19200; the calorific value may be at least 42MJ/kg e.g. at least 43.5 MJ/kg such as 42-45 or 43-45 such as 43.5-44.5MJ/kg. The gasoline usually has a boiling range (ASTM D86) of 20-225°C, in particular with at least 2% e.g. 2-15% boiling in the range 171-225°C. The gasoline is usually such that at 70°C at least 10% is evaporated while 50% is evaporated on reaching a temperature in the range 77-120°C preferably 77-116°C and by 185°C, a minimum of 90% is evaporated. The gasoline is also usually that 10-50% may be evaporated at 70°C, 40-74% at 100°C, 70-97% at 150°C and 90-99% may be evaporated at 180°C. The Reid Vapour Pressure of the gasoline at 37.8°C measured according to ASTM D323 is usually 30-120, e.g. 40-100 such as 61-80 or preferably 50-80, 40-65, e.g. 40-60 or 40-50Kpa.
  • The gasoline compositions, when free of any oxygenates usually have a H:C atom ratio of at least 1.8:1 e.g. at least 2.0:1 or at least 2.1 or 2.2:1, such as 1.8-2.3:1 or 2.0-2.2:1. Advantageously the gasoline composition meets the following criteria. Atom H:C x [1 + oxy] x [ Net Heat of Combustion 200 + ROAD] ≥ y, wherein Atom H:C is the fraction of hydrogen to carbon in the hydrocarbons in the composition, oxy means the molar fraction of oxygenate, if any in the composition, Net Heat of Combustion is the energy derived from burning 1lb (454g) weight of fuel (in gaseous form) in oxygen to give gaseous water and carbon dioxide expressed in Btu/lb units [MJ/kg times 430.35], and y is at least 350, 380, 410 or 430, in particular 350-440 e.g. 380-420 especially 400-420.
  • Preferably the motor gasoline of this invention comprises 10-90% of triptane, 10-80% of component (b), 0-25% naphtha, 0-15% of butane, 5-20% of olefin, 3-28% aromatics and 0-25% oxygenate, in particular with 5-20% aromatics and 5-15% olefins.
  • In a preferred embodiment of this invention the motor gasoline of this invention contains 8-65% of triptane (especially 15-35%), 0.1-30% such as 2-25% olefins, especially 3-14% and 0-35% aromatics such as 0-30% e.g. 5-35, 5-20 (especially 5-15%) or 20-30%, and 5-50% component (b) mixtures e.g. 10-45% such as 20-40%. Such gasolines may also contain oxygenates, such as MTBE especially in amount of less than 3% e.g. 0.1-3% and especially contain less than 1.5% benzene e.g. 0.1-1%. Such gasolines preferably have RON of 97-99, MON 87-90 and ROAD values of 92-94.5.
  • Examples of motor gasolines of the invention are ones with 5-25% triptane, 5-15% olefins, 15-35% aromatics and 40-65% component (b), in particular 15-25% triptane, 7-15%, olefins 15-25% aromatics and 45-52% component (b) mixture of RON value 96.5-97.5, or 5-15% triptane, 7-15% olefins, 15-25% aromatics and 55-65% compound (b) of RON value 94.5-95.5.
  • Examples of motor gasolines of the invention are ones having 1-15% e.g. 3-12% butane, 0-20% e.g. 5-15% ether e.g. MTBE, 20-80 e.g. 25-70% of refinery mixed liquid (usually C6-C9)streams (apart from naphtha) (such as mixtures of (i)-(iv) above), 0-25% e.g. 2-25% naphtha, 5-70% e.g. 15-65% triptane, with RON 93-100 e.g. 94-98, MON 80-98 e.g. 83-93 or 93-98, and RVP 40-80 such as 40-65Kpa. Such gasolines usually contain 1-30% e.g. 2-25% olefins and 2-30% e.g. 4-25% aromatics. Amounts of olefins of 15-25% are preferred for RON values of 94-98 e.g. 94-96 and 2-15% e.g. 2-7% for RON values of 96-100 such as 96-98.
  • Other examples of fuel compositions of the invention contain 8-18% triptane, 10-50% e.g. 25-40% of total component (b) mixture, 5-40% e.g. 20-35% of total aromatics mixture 15-60, e.g. 15-30% or 40-60% of total olefinic mixture and 0-15% total oxygenate e.g. 3-8% or 8-15%. Especially preferred compositions have 8-18% triptane, 25-40% total mixed component (b) mixture, 20-35% total aromatics, and 15-30% total olefinics, or 8-18% triptane, 15-40% total mixed component (b) mixture, 3-25% total aromatics mixture, and 40-60% total olefinic mixture.
  • Further examples of fuel compositions contain 20-40% triptane, 8-55% of the total component (b) mixture, e.g. 5-25% or 35-55%, and 0 or 5-25% e.g. 18-25% total aromatics mixture, 0-55 especially 10-55 or 40-55% total olefin mixture, especially preferred compositions having 20-40% triptane, 5-25% total component (b) mixtures, 3-25% total aromatics mixture and 40-60% total olefinic mixture, or 20-40% triptane, 35-55% total component (b) mixture 15-30% total aromatics mixture and 0-15% e.g. 5-15% total olefin mixture, or in particular 20-40% triptane, 25-45% or 30-50% total component (b) mixture, 2-15% total aromatics mixture 18-35% total olefins mixture, and especially 3-10% or 5-18% olefins, and 10-35% such as 10-20% aromatics (e.g. 10-18%).
  • Example of fuel compositions contain 30-55% e.g. 40-55% triptane, 5-30% total component (b) mixture 0-10% total aromatic mixture, 10-45% olefinic mixture and 0-15% oxygenates especially with the total of oxygenates and olefinic mixture of 20-45%. Other examples of fuel compositions contain 55-70% triptane, 10-45% total component b, e.g. 10-25% or 35-45%, and 0-10% e.g. 0 or 0.5-5% total aromatics Mixture, and 0-30% total olefinics mixtures, e.g. 0 or 15-30%, especially 55-70% triptane 10-25% total component (b) 0 or 0.5-5% total aromatics mixture and 15-30% total olefinic mixture.
  • Particularly preferred examples of fuel composition comprise 15-35% e.g. 20-35% triptane, 0-18.5% e.g. 2-18.5% olefin, 5-40% e.g. 5-35% aromatics 25-65% saturates and less than 1% benzene, and 18-65% e.g 40-65% triptane, 0-18-5% e.g. 5-18.5% olefins, 5-42% e.g. 5-28% aromatics, 35-55% saturates and less than 1% benzene.
  • Another fuel composition may comprise 25-40% e.g. 30-40% such as 35% of alkylate, 10-25% e.g. 15-25% such as 20% of isomerate, 10-25% e.g. 15-25% such as 20% of light hydrocrackate and 20-35% e.g. 20-30% such as 25% of triptane and optionally 0-5% butane. Such a composition is preferably substantially paraffinic and is substantially free of olefins and aromatics.
  • Other fuel compositions of the invention may have different ranges of the Antiknock Index (also known as The ROAD Index), which is the average of MON and RON.
  • For ROAD Indexes of 85.5-88.5, the compositions may comprise 8-30% triptane e.g. 15-30%, and 10-50% e.g. 20-40% total component (b) mixture, 5-30%, e.g. 5-20% total olefins and 10-40 e.g. 15-35% total aromatics, or 8-30% triptane, 10-50% total component (b) mixture, 5-40% total aromatic mixtures e.g. 20-30% and 10-60% e.g. 30-55% total olefinic mixtures.
  • For ROAD Indexes of 88.5-91.0 the compositions may comprise 5-25% (or 5-15%) triptane, 20-45% total component (b) mixture, 0-25% e.g. 1-10 or 10-25% total olefins, and 10-35% e.g. 10-20% or 20-35% total aromatics or 5-25% (5-15%) triptane, 20-45% total component (b) mixture, 0-35% total aromatic mixtures e.g. 1-15 or 15-35%, and 5-65% e.g. 5-30 or 30-65% total olefinic mixtures.
  • For ROAD Indexes of 91.0-94.0 the fuel compositions of the invention may comprise 5-65% e.g. 5-20, 20-30, 30-65 or 40-65% triptane and 5-40% (5-35%) e.g. 5-12 or 12-40% (12-30%) total component (b) mixture 1-30% e.g. 1-10 or 10-25% total olefins and 5-55% e.g. 5-15 or 15-35 or 35-55% total aromatics, or the above amounts of triptane with 0-55 e.g. 0.5-25% e.g. 10-25% or 25-55% of aromatic fractions and 0 or 10-60% e.g. 10-30% or 35-60% total olefin fractions.
  • For ROAD values of 94-97.9, the fuel compositions may comprise 20-65% triptane e.g. 40-65% triptane, 0-15% e.g. 5-15% total olefins, 0-20% e.g. 5-20% total aromatics and 5-50 e.g. 30-50% total component (b) mixture, or the above amounts of triptane and total component (b) mixture with 0-30% e.g. 10-30% aromatic fractions and 0-30 e.g. 5-30% olefinic fraction, or the above amounts of triptane e.g. 20-40% triptane, total component b mixture, total olefins and total aromatics, with 2-15% aromatic fractions and 18-35% olefinic fractions.
  • The invention can provide motor gasolines, in particular of 91, 95, 97, 98 and 110 RON values, with desired high Octane Levels but low emission values on combustion in particular of at least one of total hydrocarbons, total air toxics, NOx, carbon monoxide, and carbon dioxide, especially of both total hydrocarbons and NOx. Thus the invention also provides the use of a compound of formula I, in particular triptane, in unleaded motor gasoline of MON at least 80 e.g. 80 to less than 98, e.g. as an additive to or component therein, to reduce the emission levels on combustion, especially of at least one of total hydrocarbons, total air toxics NOx, carbon monoxide and carbon dioxide especially both of total hydrocarbons and NOx. The invention also provides a method of reducing emissions of exhaust gases in the combustion of unleaded motor gasoline fuels of MON of at least 80 which comprises having a compound of formula I present in the fuel which is a gasoline of the invention. The invention also provides use of an unleaded gasoline of the invention in a spark ignition combustion engine to reduce emissions of exhaust gases. While the compositions of the invention may be used in supercharged or turbocharged engines, they are preferably not so used, but are used in normally aspirated ones. The compound of formula I e.g. triptane can reduce one or more of the above emission levels better than amounts of alkylate or a mixture of aromatics and oxygenate at similar Octane Number and usually decrease the fuel consumption as well.
  • The present invention is illustrated in the following Examples.
  • Examples 1-6
  • In these Examples 2,2,3 trimethylbutane (triptane) 99% purity was mixed with various refinery fractions and butane, and optionally methyl tertiary butyl ether, to produce a series of gasoline blends, for making unleaded motor gasolines.
  • Formulated gasolines were made by mixing each blend with a phenolic antioxidant 55% minimum 2,4 dimethyl-6-tertiary butyl phenol 15% minimum 4 methyl-2, 6-ditertiary-butyl phenol with the remainder as a mixture of monomethyl and dimethyl-tertiary butyl phenols.
  • In each case the gasolines were tested for MON and RON, and their Reid Vapour Pressure at 37.8°C and their calorific value, and their distillation properties. The results are shown in table 1.
    Example 1 2 3 4 5 6
    Composition % v/v
    Triptane 10.0 50.0 50.0 25.0 25.0 60.0
    Butane 10.0 5.0 5.0 5.0 5.0 5.0
    Mixed Fractions (apart from 60.0 30.0 30.0 65.0 50.0 35.0
    Naphtha) of which
    Catalytic reformate 5.0 0 0 18.1 0 1.3
    HCC 6.48 18.62 17.68 0 9.31 22.73
    LCC 48.52 0 19.05 46.90 36.41 0.00
    SRG 0 11.38 3.27 0 4.28 10.85
    Isopentane 0 0 0 0 0 0.12
    Naphtha 20.0 5.0 5.0 5.0 20.0 0.00
    MTBE 0 10.0 0 0 0 0
    Analysis, %v/v
    Aromatics 14.1 6.3 8.5 19.1 10.0 7.9
    Olefins 23.5 3.2 11.7 21.4 18.5 3.8
    Antioxidant mg/l 15 15 15 15 15 15
    Distillation °C
    T 10% 43.6 58.0 58.4 51.2 54.0 60.0
    T 50% 89.1 93.2 97.1 85.5 91.9 99.2
    T 90% 154.0 177.8 176.9 140.4 159.0 185.0
    Reid Vapour Pressure kPa 78.1 46.9 47.4 63.9 57.3 42.9
    RON 95.0 97.3 97.0 97.0 95.0 99.4
    MON 85.9 97.2 95.4 90.0 89.0 87.3
    ROAD 90.45 97.25 96.2 93.5 92.0 93.35
  • In the above table mixed fractions means a blend of refinery fractions in which HCC is heavy catalytically cracked spirit, LCC is light catalytically cracked spirit and SRG is straight run gasoline.
  • Example 7
  • The combustion characteristics of the gasolines of Ex. 1-6 were tested against standard unleaded gasolines. Combustion of the gasolines of Ex.1-6gave less carbon dioxide emissions than from equal volumes of the standard gasolines of similar ROAD Octane Number.
  • Example 8 and Comparative Ex A-C
  • The emission characteristics on combustion of a series of gasoline fuels with 25% of different components were compared, the components being heavy reformate (comp A), triptane (Ex8), alkylate (comp B) and a mix of 10% heavy reformate and 15% MTBE (comp C). The gasoline fuels and their properties were as follows. Formulated gasolines were made by addition of the phenolic antioxidant in amount and nature as in Ex1-7.
    Example A 8 B C
    Composition
    Butane 3 3 3 3
    Reformate 22 22 22 22
    Alkylate 40 40 65 40
    Bisomer ('CCS') 10 10 10 10
    Heavy Reformate 25 10
    Triptane 25
    MTBE 15
    Density kg/1 0.7623 0.7163 0.7191 0.7424
    RON 101.2 100.2 98.5 101.1
    MON 89.4 93.2 88.3 90.2
    ROAD 95.3 96.7 93.4 95.65
    %Aromatics 38.9 13.9 13.9 23.9
    % Olefins 10.2 10.2 10.2 10.2
    % Saturates 50.9 75.9 75.9 65.9
    % Benzene 0.9 0.9 0.9 0.9
  • The fuels were tested in a single cylinder research engine at a number of different engine settings. The speed/load was 20/7.2 rps/Nm/, or 50/14.3 rps/Nm the LAMBDA setting was 1.01 or 0.95, and the ignition setting was set or optimized. The emissions of CO, CO2 , total hydrocarbons, NOx, and total air toxics (benzene, butadiene, formaldehyde and acetaldehyde) were measured from the exhaust gases. The results from the different engine settings were averaged and showed that, compared to the base blend (Comp. Ex. A) the emissions with the compositions containing heavy reformate and MTBE (Comp. C), 25% alkylate (Comp. B) and 25% triptane (Ex8) were reduced, the degrees of change being as follows.
    Example % CO %CO2 %THC %NOx %TAT %FC
    Comp C (MTBE -4.9 -2.3 -6.2 -6.5 -9.2 +1.4
    Comp B (alkylate) -7.9 -4.5 -4.0 -8.0 -13.1 -2.9
    8 /triptane -9.6 -5.6 -6.6 -10.1 -18.7 -4.1
    Where THC is total hydrocarbons, TAT is total air toxics. The Fuel Consumption (FC) was also measured in g/kWhr and the change relative to the base blend are also shown in Table 2.
  • Example 9-22
  • Gasolines were made up as in Ex 1-6 from components as shown in the table below, and had the properties shown. They gave low carbon dioxide emissions.
    Figure 00150001
    Figure 00160001
  • Examples 24-8 and Comparative Example D
  • Emission characteristics were obtained as in Ex.8 (apart from Lamba settings of 1.00 and 0.95 set for the base fuel (Comp.D) on combustion of a series of gasoline fuels with different components namely reformate, (high aromatics), (Comp.D), triptane, Ex.24-27 and triptane/ethanol Ex.28. Fuel consumption was also measured in g/kWhr. Formulated gasolines were made by addition of the phenolic antioxidant in amount and nature as in Ex.1-7. The compositions were as shown in Table 3. The results were expressed in Table 4 as the percentage change in emissions or in fuel consumption compared to Ex.D.
    Example 24 25 26 27 28 D
    Composition % v/v
    Triptane 40 10 25 60 10
    Butane 2.96 2.96 2.96 2.96 2.96
    Mixed Fractions (apart from 87.04 72.04 37.04
    Naphtha) of which
    Catalytic reformate 19.78 4.78 21.28 25.25
    CCS 5 5 5 5 10 5
    Steam cracked spirit 37.2 47.42 47.42 17.2 9.7 47.42
    SRG 15.72
    Toluene 4.53
    Naphtha 13.79
    Ethanol 5
    Heavy reformate 9.51
    Cyclohexane 5 5 5 5 5 5
    Light hydrocrackate 7.93 7.93 7.93 7.93 7.93
    C6 Bisomer 1.91 1.91 1.91 1.91 1.91
    Analysis, %v/v
    Aromatics 15.0 31.2 21.7 7.8 31.1 39.2
    Olefins 13.4 16.2 16.1 8.3 6.5 16.2
    Sulphur % w/w 0.007 0.007 0.007 0.007 0.012 0.007
    Antioxidant mg/l 10 10 10 10 10 10
    Distillation °C %
    T 10%
    T 50%
    T 90%
    Reid Vapour Pressure kPa
    RON 98.7 96.8 97.5 101.0 93.2 96.6
    MON 86.1 82.8 83.7 89.6 82.4 82.5
    ROAD 92.4 89.8 90.6 95.3 88.1 89.55
    Example % CO % CO2 % THC % NOx % TAT % Fuel Composition
    25 -3.3 -2.1 -4.7 -4.0 -5.0 -1.4
    26 -8.6 -3.8 -8.7 -7.0 -19.1 -2.5
    27 -17.4 -6.8 -10.5 -18.0 -35.3 -4.5
    24 -14.9 -5.0 -7.9 -12.2 -28.7 -3.4
    28 -11.7 -2.2 -3.2 -10.3 -10.1 +0.1
    Example F.G 29
    Composition % v/v
    Triptane 25
    Butane 0.75 0
    Mixed Fractions (apart from Naphtha) of which
    Catalytic reformate * 11.0 7.5
    Steam cracked spirit * 31.5 30.0
    Alkylate 40.9 37.5
    Toluene 15.8 0
    Analysis, %v/v
    Aromatics 34.2 15.6
    Olefins 8.2 7.8
    Saturates 57.6 76.6
    Sulphur ppm 7.3 10
    Benzene %w/w 0.75 0.64
    Antioxidant mg/l 10 10
    Distillation % Evap. 70°C 18.8 21.6
    E % 100°C 44.4 64.5
    E % 150°C 92.8 93.3
    E % 180°C 96.4 98
    Reid Vapour Pressure kPa 56.8 52.2
    RON 99.5 99.7
    MON 87.6 89.3
    ROAD 93.05 94.5
  • Examples 29 and Comparative Ex. F, G
  • 3 gasoline fuels (Ex.29, F and G) were compared for production of emissions on combustion in cars. The gasoline fuels had the compositions and properties as shown in Table 5 and the formulated gasolines included antioxidant as in Ex.1. The fuels met the requirements of 2005 Clean Fuel specification according to Directive 98/70 EC Annexe 3. The cars were regular production models, namely 1998 Ford Focus (1800cc), 1996-7 VW Golf (1600cc), 1998 Vauxhall Corsa (1000cc), 1994-5 Peugeot 106 (1400cc) and 1998 Mitsubishi GDI (1800cc) each fitted with a catalytic converter. The Corsa had 3 cylinders, the rest 4 cylinders, while the 106 had single point injection; the Mitsubishi had direct injection and the rest multipoint injection for their combustion.
  • 2 separate base fuel experiments (comp F & G) were done. The emissions were tested in triplicate in a dynamometer on the European Drive Cycle test as described in the MVEG test cycle (EC.15.04+EUDC) modified to start sampling on cranking and 11 sec. Idle as given in Directive 98/69 EC (the disclosure of which is hereby incorporated by reference). The EDC test over 11km comprises the ECE cycle (City driving test) repeated 4 times followed by the Extended Urban Drive Cycle test (incorporating some driving at up to 120km/hr). The emissions were measured out of the engine (i.e. upstream of the catalytic converter) and also as tailpipe emissions (i.e. downstream of the converter) and were sampled every second (except for the Focus) and cumulated over the test, the results being expressed as g emission per km travelled. The emissions of the first ECE cycle with the Focus were not measured. The emissions tested were for the total hydrocarbons, CO2, CO and NOx and the fuel consumption was determined on a gravimetric basis. The geometric means of the emission and consumption results across the 5 cars were obtained. The values for the Comparative fuels were averaged.
  • In the following tests, the CO2 emissions averaged over the 5 cars were lower with the triptane fuel (Ex.29) compared to the averaged base fuel results (Comp.F, G), namely Total tailpipe emissions in EDC tests, EUDC test and ECE test, the reductions being respectively 2.8%, 2.7% and 2.8%. The Fuel Consumptions averaged over the 5 cars were lower with the triptane fuel (Ex.29) compared to the averaged base results (Comp.F, G) in those same tests, the reductions being respectively, 0.6%, 0.6% and 0.5%. The tailpipe emissions results for THC, CO and NOx in at least some parts of the total EDC cycle showed trends towards triptane giving lower emissions than the base fuel, but the differences may or may not be confirmed in view of the limited number of vehicles tested.
  • The ECE tests simulates city driving and has 4 identical repeats of a specified speed profile, which profile has 3 progressively higher speed sections interspersed by zero speed sections (the average speed being 19km/hr). The first profile corresponds to driving from a cold start. In a cold engine, the effects of friction, lubricants and the nature of the fuel among others, differ from those with a hot engine in an unpredictable way, and it is with cold engines that most tailpipe emissions are produced, because the catalytic converter becomes increasingly effective at reducing emissions when it becomes hot. In addition a Lambda sensor upstream of the converter controls the fuel/air ratio entering the engine, but this is not effective with a cold engine (resulting in an unregulated fuel/air ratio); after cold start the sensor quickly becomes effective, (resulting in a regulated fuel/air ratio), even when the catalyst is not yet hot enough to be effective. Thus cold start operations are different from hot running operations and yet contribute to a large amount of tailpipe emissions.
  • The out of engine results from the first profile ECE tests (simulating cold start) with the above fuels (Ex.29 and Comp.F, G) were the same as the tailpipe emissions as the catalyst was not effective then. The results in these cold start tests for CO2, HC, CO and NOx averaged over the Golf, Corsa, Peugeot and Mitsubishi, and also averaged over the Golf, Corsa and Peugeot showed trends toward triptane giving lower emissions than the base fuel, but the differences may or may not be confirmed in view of the limited number of vehicles tested.
  • This period of cold start simulated as above may correspond in real life to a period of time or distance, which may vary, depending on how the car is driven and/or ambient conditions e.g. up to 1 km or 4 or 2 min, or a temperature of the engine coolant (e.g. radiator water temperature) of up to 50°C. The car engine may also be deemed cold if it has not been operated for the previous 4hr before start, usually at least 6hr before start.
  • Thus the present invention also provides of method of reducing emissions of exhaust gases in the combustion of unleaded gasoline fuels of MON of at least 80 e.g. 80 to less than 98 from cold start of a spark ignition combustion engine, which comprises having a compound of formula I present in the fuel which is a gasoline of the invention.

Claims (46)

  1. An unleaded formulated motor gasoline having a MON of 80 to less than 98 comprising a base blend composition having a Motor Octane Number (MON) of at least 80 comprising component (a) at least 5% (by volume of the total composition) of at least one hydrocarbon having the following formula I R-CH2-CH(CH3)-C(CH3)2-CH3 wherein R is hydrogen or methyl
    and component (b) at least one saturated liquid aliphatic hydrocarbon having 4 to 12 carbon atoms, and at least one motor gasoline additive selected from anti-oxidants, corrosion inhibitors, anti-icing additives, engine detergent additives, anti-static additives, metal deactivators, surface ignition inhibitors, combustion improvers, anti valve seat recession additives and colouring agents.
  2. A gasoline according to claim 1 wherein said composition has a MON value of 80 to less than 98 and said saturated hydrocarbon has 4 to 10 carbons.
  3. A gasoline according to claim 2 which comprises as component (a) at least 8% by volume of triptane and said saturated hydrocarbon has 5 to 10 carbon atoms.
  4. A gasoline according to any preceding claim wherein component (b) is contained in at least one of isomerate, alkylate, straight run gasoline, light reformate, light hydrocrackate and aviation alkylate.
  5. A gasoline according to claim 4 wherein said composition comprises at least 8% by volume of triptane and wherein component (b) is at least one of isomerate, alkylate, aviation alkylate and straight run gasoline and comprises at least one saturated liquid aliphatic hydrocarbon having 5-10 carbon atoms.
  6. A gasoline according to any one of the preceding claims wherein said composition comprises at least one saturated aliphatic hydrocarbon having 4-6 carbons, which has a lower boiling point than triptane and has a Motor Octane Number greater than 88.
  7. A gasoline according to any one of the preceding claims wherein said composition comprises at least one saturated aliphatic hydrocarbon having 5-10 carbon atoms, which has a higher boiling point than triptane and has a Motor Octane Number greater than 92.
  8. A gasoline according to any one of the preceding claims wherein said composition comprises at least one olefin which is an alkene of 5-10 carbons, with a MON value of 70-90 in amount of 1-30% by volume.
  9. A gasoline according to claim 8 wherein said composition comprises said alkene in amount of 5-20% by volume.
  10. A gasoline according to any one of the preceding claims wherein said composition comprises at least one of catalytically cracked spirit, steam cracked spirit, C6 bisomer, catalytic polymerate and dimate.
  11. A gasoline according to claim 10 wherein said composition comprises catalytically cracked spirit.
  12. A gasoline according to any one of the preceding claims wherein said composition also comprises at least one aromatic compound of MON value 90-110, in amount of 2-40% (by volume).
  13. A gasoline according to claim 12 wherein said composition comprises at least one aromatic compound of MON value 90-110 in amount of 3-28% by volume.
  14. A gasoline according to any one of the preceding claims wherein said composition also comprises at least one aromatic compound added as single compounds or added as an aromatic mixture made from catalytically reformed or cracked gasoline obtained from heavy naphtha.
  15. A gasoline according to any one of the preceding claims wherein said composition also comprises at least one oxygenate octane booster of MON value of at least 96-105 in amount of 1-25% by volume.
  16. A gasoline according to any of the preceding claims wherein said composition has a Reid Vapour pressure at 37.8°C measured according to ASTM D323 of 40-100kPa.
  17. A gasoline according to any one of the preceding claims wherein said composition meets the following criterion Atom H:C x [1 + oxy] x [Net Heat of Combustion200 + ROAD] ≥ y, wherein Atom H:C is the fraction of hydrogen to carbon in the hydrocarbons in the composition, oxy means the molar fraction of oxygenate, if any, in the composition, Net Heat of Combustion is the energy derived from burning 11b (454g) weight of fuel (in gaseous form) in oxygen to give gaseous water and carbon dioxide expressed in Btu/1b units [MJ/kg times 430.35], and y is at least 350 in particular 350-440, and ROAD is the average of Motor Octane Number and Research Octane Number.
  18. A gasoline according to any one of the preceding claims wherein said composition comprises (by volume) 10-90% of triptane, 10-80% of component (b), 0-25% naphtha, 0-15% of butane, 0-20% of olefin, 3-28% aromatics and 0-25% oxygenate.
  19. A gasoline according to any one of the preceding claims wherein said composition comprises 5-20% aromatics, and 5-18.5% olefins (by volume).
  20. A gasoline according to any one of claims 1-17, wherein said composition comprises (by volume) 8-65% of triptane, 0.1-30% olefins and 5-35% aromatics, 5-50% component (b) mixtures, oxygenates, in amount of less than 3% and less than 1.5% benzene, and having RON of 97-99, MON 87-90 and ROAD values of 92-94.5.
  21. A gasoline according to claim 20, wherein said composition comprises (by volume) 15-35% of triptane, 2-25% olefins and/or 0.1-1% benzene.
  22. A gasoline according to claim 20 or claim 21, wherein said composition comprises (by volume) 3-14% olefins.
  23. A gasoline according to any one of claims 1-17, wherein said composition comprises (by volume) 5-25% triptane, 5-15% olefins, 15-35% aromatics and 40-65% component (b), in particular 15-25% triptane, 7-15% olefins, 15-25% aromatics and 45-52% component (b) mixture and of RON value 96.5-97.5.
  24. A gasoline according to any one of claims 1-17, wherein said composition comprises (by volume) 1-15% butane, 0-20% MTBE, 20-80% of refinery mixed liquid C6-C9 streams (apart from naphtha) 0-25% naphtha, 15-65% triptane, with RON 93-100, MON 80-98, and RVP 40-80kPa, with 1-30% olefins and 2-30% aromatics.
  25. A gasoline according to any one of claims 1-17 wherein said composition comprises (by volume) 8-18% triptane, 10-50% e.g. 25-40% of total component (b) mixture, 5-40% e.g. 20-35% of total aromatics mixture, 15-30% of total olefinic mixture and 0-15% total oxygenate.
  26. A gasoline according to any one of claims 1-17 wherein said composition comprises (by volume) 20-40% triptane, 8-55% of the total component (b) mixture, 5-25% total aromatics mixture, and 10-55% total olefin mixture.
  27. A gasoline according to any one of claims 1-17 wherein said composition comprises (by volume) 40-55% triptane, 5-30% total component (b) mixture, 0-10% total aromatic mixture, 10-45% olefinic mixture and 0-15% oxygenates, with the total of oxygenates (if any) and olefinic mixture of 20-45%.
  28. A gasoline according to any one of claims 1-17 wherein said composition comprises (by volume) 55-70% triptane, 10-45% total component (b), and 0-10% total aromatics Mixture, and 0-30% total olefinics mixtures, especially 55-70% triptane, 10-25% total component (b), 0 or 0.5-5% total aromatics mixture and 15-30% total olefinic mixture.
  29. A gasoline according to any one of claims 1-17 wherein said composition has a ROAD Index, which is the average of MON and RON, of 85.5-88.5, and comprises (by volume) 8-30% triptane and 10-50% total component (b) mixture, 5-30% total olefins and 10-40% total aromatics.
  30. A gasoline according to any one of claims 1-17 wherein said composition has a ROAD Index of 88.5-91.0 and comprises (by volume) 5-25% triptane, 20-45% total component (b) mixture, 1-25% total olefins, and 10-35% e.g. 10-20% or 20-35% total aromatics.
  31. A gasoline according to any one of claims 1-17 wherein said composition has a ROAD Index of 91.0-94.0, and comprises (by volume) 5-65% triptane and 5-40% total component (b) mixture, 1-30% total olefins and 5-55% total aromatics.
  32. A gasoline according to any one of claims 1-17 wherein said composition has a ROAD Index of 94-97.9, and comprises (by volume) 20-65% triptane, 5-15% total olefins, 5-20% total aromatics and 5-50% total component (b) mixture.
  33. A gasoline according to any one of claims 1-17 wherein said composition comprises (by volume) 15-35% triptane, 0-18.5% olefin, 5-40% aromatics and 25-65% saturates and has less than 1% benzene.
  34. A gasoline according to any one of claims 1-17 wherein said composition comprises (by volume) 40-65% triptane, 5-18.5% olefins, 5-28% aromatics and 35-55% saturates and less than 1% benzene.
  35. A gasoline according to any one of claims 1-34 wherein said motor gasoline additive is an anti-oxidant, corrosion inhibitor, anti-icing additive, engine detergent additive or anti-static additive, or mixture thereof.
  36. A gasoline according to claim 35 wherein the additive is an antioxidant.
  37. An unleaded motor gasoline base blend composition as defined in any one of claims 2 to 34, and wherein the composition contains the hydrocarbon of formula I in an amount of up to 40% by volume, and wherein said composition further comprises at least one aromatic compound of MON value 90-110 in an amount of 2-40% (by volume).
  38. A composition according to claim 37 which also comprises at least one of an olefin of 5-10 carbon atoms, aromatic compound in amount of 1-28% or contains less than 5% (by volume) of benzene.
  39. A composition according to any one of claims 37-38 which comprises said olefin and 1-35% aromatics (by volume).
  40. A composition according to any one of claims 37-39 which comprises at least 8% of triptane, component (b) comprising said hydrocarbon of 5 to 10 carbon atoms, and a liquid alkene of 5-10 carbon atoms, and optionally butane.
  41. A composition according to any one of claims 37-40 which comprises (by volume) 10-40% triptane and less than 5% benzene, and has a Reid Vapour Pressure at 37.8°C measured according to ASTMD323 of 30-120kPa.
  42. A composition according to any one of claims 37-41 which comprises at least one of isomerate, alkylate, and straight run gasoline, which contains component (b).
  43. A composition according to any one of claims 37-42 which also comprises at least one saturated aliphatic hydrocarbon having 4-6 carbons which has a boiling point at atmospheric pressure at least 30°C lower than the hydrocarbon of formula I.
  44. A method of reducing emissions of exhaust gases in the combustion of unleaded motor gasoline fuels of MON of at least 80 which comprises having a compound of formula I as defined in claim 1 present in the fuel which is a gasoline as claimed in any one of claims 1-36.
  45. A method of reducing emissions of exhaust gases in the combustion of unleaded gasoline fuels of MON of at least 80, for example 80 to less than 98, from cold start of a spark ignition combustion engine, which comprises having a compound of formula I as defined in claim 1 present in the fuel which is a gasoline as claimed in any one of claims 1 to 36.
  46. A gasoline as claimed in any one of claims 1 to 36, or a composition as claimed in any one of claims 37 to 43 or a method as claimed in any one of claims 44 to 45 in which the compound of formula I is triptane.
EP03076773A 1998-03-26 1999-03-26 Fuel composition Expired - Lifetime EP1359207B1 (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
GBGB9806440.5A GB9806440D0 (en) 1998-03-26 1998-03-26 Fuel composition
GB9806440 1998-03-26
GBGB9822277.1A GB9822277D0 (en) 1998-10-14 1998-10-14 Fuel composition
GB9822277 1998-10-14
EP99913461A EP1068282B1 (en) 1998-03-26 1999-03-26 Use of an additive in a fuel composition

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EP1359207A1 true EP1359207A1 (en) 2003-11-05
EP1359207B1 EP1359207B1 (en) 2007-01-17

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Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2005118751A1 (en) * 2004-05-26 2005-12-15 Shell Internationale Research Maatschappij B.V. Aliphatic gasoline component and process to prepare said gasoline component
CN100575460C (en) * 2004-05-26 2009-12-30 国际壳牌研究有限公司 The method of aliphatic series gasoline component and the described gasoline component of preparation
WO2010014501A1 (en) * 2008-07-28 2010-02-04 Shell Oil Company High octane unleaded fuel compositions and methods for increasing the maximum torque output value produced burning same
US7667086B2 (en) 2005-01-31 2010-02-23 Exxonmobil Chemical Patents Inc. Olefin oligomerization and biodegradable compositions therefrom
US7678953B2 (en) 2005-01-31 2010-03-16 Exxonmobil Chemical Patents Inc. Olefin oligomerization
US7678954B2 (en) 2005-01-31 2010-03-16 Exxonmobil Chemical Patents, Inc. Olefin oligomerization to produce hydrocarbon compositions useful as fuels
US7692049B2 (en) 2005-01-31 2010-04-06 Exxonmobil Chemical Patents Inc. Hydrocarbon compositions useful for producing fuels and methods of producing the same
US7741526B2 (en) 2006-07-19 2010-06-22 Exxonmobil Chemical Patents Inc. Feedstock preparation of olefins for oligomerization to produce fuels
US20120080000A1 (en) * 2006-12-12 2012-04-05 Shell Oil Company Unleaded fuel compositions
US8481796B2 (en) 2005-01-31 2013-07-09 Exxonmobil Chemical Patents Inc. Olefin oligomerization and compositions therefrom
US8741126B2 (en) 2008-06-30 2014-06-03 Total Marketing Services Aviation gasoline for aircraft piston engines, preparation process thereof
US9163189B2 (en) 2011-12-01 2015-10-20 Shell Oil Company Balanced unleaded fuel compositions
US11193077B1 (en) 2013-03-13 2021-12-07 Airworthy Autogas, Llc Gasoline for aircraft use

Families Citing this family (28)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080172931A1 (en) 1996-11-18 2008-07-24 Bp Oil Internationa Limited Fuel composition
US7462207B2 (en) 1996-11-18 2008-12-09 Bp Oil International Limited Fuel composition
AU765382C (en) * 1999-06-11 2004-09-02 Bp Oil International Limited Fuel composition
GB2360042A (en) 2000-03-10 2001-09-12 Exxonmobil Res & Eng Co Low sulphur fuel composition
GB0121105D0 (en) 2001-08-31 2001-10-24 Bp Oil Int An improved process for the production of triptane
US7540887B1 (en) 2002-07-23 2009-06-02 Gregory Turocy Methods and systems for producing fuel compositions
GB0226587D0 (en) * 2002-11-14 2002-12-24 Bp Oil Int Aviation gasoline composition, its preparation and use
US7416568B2 (en) 2002-11-14 2008-08-26 Bp Oil International Limited Aviation gasoline composition, its preparation and use
EP2060550A1 (en) 2007-11-16 2009-05-20 BP p.l.c. Process for producing triptane
EP2060551A1 (en) 2007-11-16 2009-05-20 BP p.l.c. Process for producing triptane
US9963652B1 (en) * 2009-07-29 2018-05-08 The United States Of America As Represented By The Secretary Of The Navy High density cyclic fuels derived from linear sesquiterpenes
US8679204B2 (en) * 2009-11-17 2014-03-25 Shell Oil Company Fuel formulations
US8628594B1 (en) 2009-12-01 2014-01-14 George W. Braly High octane unleaded aviation fuel
US10260016B2 (en) 2009-12-01 2019-04-16 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
US8324437B2 (en) 2010-07-28 2012-12-04 Chevron U.S.A. Inc. High octane aviation fuel composition
JP6782694B2 (en) 2014-07-14 2020-11-11 スウィフト・フュエルス・エルエルシー Aviation fuel with renewable oxygenated material
WO2016010952A1 (en) * 2014-07-14 2016-01-21 Swift Fuels, Llc Unleaded gasoline formulations for piston engines
FI20165785A (en) * 2016-10-13 2018-04-14 Neste Oyj Alkylaattibensiinikoostumus
MX2018014994A (en) 2016-10-18 2019-05-13 Mawetal Llc Polished turbine fuel.
CN114774163B (en) 2016-10-18 2024-01-19 马威特尔有限责任公司 Formulated composition for use as fuel
KR102279995B1 (en) 2016-10-18 2021-07-20 모에탈 엘엘씨 Environment-friendly marine fuel
RU2656850C1 (en) * 2017-06-14 2018-06-07 Общество с ограниченной ответственностью "ЛУКОЙЛ-Нижегороднефтеоргсинтез" (ООО "ЛУКОЙЛ-Нижегороднефтеоргсинтез") Composition of motor petrol
US10377959B2 (en) 2017-08-28 2019-08-13 General Aviation Modifications, Inc. High octane unleaded aviation fuel
US10364399B2 (en) 2017-08-28 2019-07-30 General Aviation Modifications, Inc. High octane unleaded aviation fuel
RU2709515C1 (en) * 2019-03-22 2019-12-18 Маветал Ллс Fuel composition formed from light oil of low-permeability reservoir and fuel oils with high content of sulfur
FR3122435B1 (en) * 2021-04-30 2023-05-12 Total Marketing Services Fuel composition rich in aromatic compounds and oxygenated compounds
FR3122434B1 (en) * 2021-04-30 2024-06-14 Total Marketing Services Fuel composition rich in aromatic compounds, paraffins and ethanol, and its use in particular in competition vehicles

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4059646A (en) * 1975-10-02 1977-11-22 Shell Oil Company Process for producing triptane by contacting methanol or dimethyl ether with zinc bromide
GB2106933A (en) * 1981-07-31 1983-04-20 Aldon Automotive Limited Additives for improving the octane rating of liquid motor fuels
WO1998022556A1 (en) * 1996-11-18 1998-05-28 Bp Oil International Limited Fuel composition

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4059646A (en) * 1975-10-02 1977-11-22 Shell Oil Company Process for producing triptane by contacting methanol or dimethyl ether with zinc bromide
GB2106933A (en) * 1981-07-31 1983-04-20 Aldon Automotive Limited Additives for improving the octane rating of liquid motor fuels
WO1998022556A1 (en) * 1996-11-18 1998-05-28 Bp Oil International Limited Fuel composition

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100575460C (en) * 2004-05-26 2009-12-30 国际壳牌研究有限公司 The method of aliphatic series gasoline component and the described gasoline component of preparation
US8974659B2 (en) 2004-05-26 2015-03-10 Shell Oil Company Aliphatic gasoline component and process to prepare said gasoline component
WO2005118751A1 (en) * 2004-05-26 2005-12-15 Shell Internationale Research Maatschappij B.V. Aliphatic gasoline component and process to prepare said gasoline component
US8481796B2 (en) 2005-01-31 2013-07-09 Exxonmobil Chemical Patents Inc. Olefin oligomerization and compositions therefrom
US7667086B2 (en) 2005-01-31 2010-02-23 Exxonmobil Chemical Patents Inc. Olefin oligomerization and biodegradable compositions therefrom
US7678953B2 (en) 2005-01-31 2010-03-16 Exxonmobil Chemical Patents Inc. Olefin oligomerization
US7678954B2 (en) 2005-01-31 2010-03-16 Exxonmobil Chemical Patents, Inc. Olefin oligomerization to produce hydrocarbon compositions useful as fuels
US7692049B2 (en) 2005-01-31 2010-04-06 Exxonmobil Chemical Patents Inc. Hydrocarbon compositions useful for producing fuels and methods of producing the same
US7741526B2 (en) 2006-07-19 2010-06-22 Exxonmobil Chemical Patents Inc. Feedstock preparation of olefins for oligomerization to produce fuels
US20120080000A1 (en) * 2006-12-12 2012-04-05 Shell Oil Company Unleaded fuel compositions
US9074153B2 (en) 2006-12-12 2015-07-07 Shell Oil Company Unleaded fuel compositions
US8741126B2 (en) 2008-06-30 2014-06-03 Total Marketing Services Aviation gasoline for aircraft piston engines, preparation process thereof
WO2010014501A1 (en) * 2008-07-28 2010-02-04 Shell Oil Company High octane unleaded fuel compositions and methods for increasing the maximum torque output value produced burning same
US9163189B2 (en) 2011-12-01 2015-10-20 Shell Oil Company Balanced unleaded fuel compositions
US11193077B1 (en) 2013-03-13 2021-12-07 Airworthy Autogas, Llc Gasoline for aircraft use
US11485923B1 (en) 2013-03-13 2022-11-01 Airworthy Autogas, Llc Gasoline for aircraft use

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PT1359207E (en) 2007-04-30
DE69912757D1 (en) 2003-12-18
DE69934918D1 (en) 2007-03-08
GB2350372A (en) 2000-11-29
MY119842A (en) 2005-07-29
WO1999049003A1 (en) 1999-09-30
TW445294B (en) 2001-07-11
EP1068282A1 (en) 2001-01-17
DE69934918T2 (en) 2007-11-08
NZ507073A (en) 2002-12-20
ES2279926T3 (en) 2007-09-01
CN1301291A (en) 2001-06-27
GB2350372B (en) 2002-09-18
AR014789A1 (en) 2001-03-28
ATE254160T1 (en) 2003-11-15
CN1160442C (en) 2004-08-04
EP1359207B1 (en) 2007-01-17
AU753443B2 (en) 2002-10-17
EG22450A (en) 2003-02-26
GB0022591D0 (en) 2000-11-01
ATE351896T1 (en) 2007-02-15
ES2212545T3 (en) 2004-07-16
CA2325748A1 (en) 1999-09-30
ID26367A (en) 2000-12-14
EP1068282B1 (en) 2003-11-12
PA8469901A1 (en) 2000-09-29
AU753443C (en) 2003-05-15
PE20000343A1 (en) 2000-05-04
DE69912757T2 (en) 2004-05-27
AU3158099A (en) 1999-10-18

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