US20030159340A1 - Gasoline compositions - Google Patents

Gasoline compositions Download PDF

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US20030159340A1
US20030159340A1 US10/364,934 US36493403A US2003159340A1 US 20030159340 A1 US20030159340 A1 US 20030159340A1 US 36493403 A US36493403 A US 36493403A US 2003159340 A1 US2003159340 A1 US 2003159340A1
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group
range
ppmw
moiety
gasoline
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Christopher Clayton
David Kendall
David Martin
Richard Price
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Shell USA Inc
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Assigned to SHELL OIL COMPANY reassignment SHELL OIL COMPANY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CLAYTON, CHRISTOPHER WILLIAM, KENDALL, DAVID ROY, MARTIN, DAVID PHILIP, PRICE, RICHARD JOHN
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/143Organic compounds mixtures of organic macromolecular compounds with organic non-macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/16Hydrocarbons
    • C10L1/1625Hydrocarbons macromolecular compounds
    • C10L1/1633Hydrocarbons macromolecular compounds homo- or copolymers obtained by reactions only involving carbon-to carbon unsaturated bonds
    • C10L1/1641Hydrocarbons macromolecular compounds homo- or copolymers obtained by reactions only involving carbon-to carbon unsaturated bonds from compounds containing aliphatic monomers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/188Carboxylic acids; metal salts thereof
    • C10L1/1881Carboxylic acids; metal salts thereof carboxylic group attached to an aliphatic carbon atom
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/198Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
    • C10L1/1985Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid polyethers, e.g. di- polygylcols and derivatives; ethers - esters
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/222Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
    • C10L1/2222(cyclo)aliphatic amines; polyamines (no macromolecular substituent 30C); quaternair ammonium compounds; carbamates
    • C10L1/2225(cyclo)aliphatic amines; polyamines (no macromolecular substituent 30C); quaternair ammonium compounds; carbamates hydroxy containing
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/238Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/238Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/2383Polyamines or polyimines, or derivatives thereof (poly)amines and imines; derivatives thereof (substituted by a macromolecular group containing 30C)

Definitions

  • This invention relates to gasoline compositions, more particularly to such compositions containing a fatty acid salt of an alkoxylated oligoamine, and their preparation.
  • U.S. Pat. No. 4,131,583 discloses certain fatty acid salts of alkoxylated oligoamines and their use as corrosion inhibitors in aqueous coating agents for metal surfaces.
  • each moiety A independently represents an alkylene group of 2 to 8 carbon atoms
  • each moiety R independently represents a C 7-23 alkyl or singly or multiply-unsaturated C 7 to C 23 alkenyl group, optionally substituted by one or more —OH groups
  • each moiety Z independently represents a C 1-8 alkylene group, a C 3-8 cycloalkylene group or a C 6-12 arylene or arylalkylene group
  • m represents 0 or an integer in the range 1 to 5
  • the total of all variables x has a value of 50% to 300% of (m+3), as lubricity improvers for mineral oil products, including fuels and lubricating oils.
  • Example 3 in DE-A-19955651 specifically describes the advantageous lubricity properties of a composition based on a 50% distillation residue of a standard Eurosuper gasoline into which was incorporated 50 mg/kg (ppmw) of a specific salt of formula I and 500 mg/kg (ppmw) of an additive package containing a polyisobutylene amine detergent, a synthetic carrier oil and a conventional corrosion inhibitor. These lubricity properties are demonstrated in a high frequency reciprocating rig (HFFR) test.
  • HFFR high frequency reciprocating rig
  • a gasoline composition comprising a major amount of a gasoline suitable for use in a spark ignition engine; 5 to 1000 ppmw, based on total composition, of a fatty acid salt of an alkoxylated oligoamine of general formula I
  • each moiety A independently represents an alkylene group of 2 to 8 carbon atoms
  • each moiety R independently represents a C 7-23 alkyl or singly or multiply-unsaturated C 7 to C 23 alkenyl group, optionally substituted by one or more —OH groups
  • each moiety Z independently represents a C 1-8 alkylene group, a C 3-8 cycloalkylene group, or a C 6-12 arylene or arylalkylene group
  • m represents 0 or an integer in the range 1 to 5
  • the total of all variables x has a value of 50% to 300% of (m+3)
  • 600 to 2000 ppmw based on total composition, of a co-additive selected from the group consisting of (a) a nitrogen-containing detergent containing a hydrocarbyl group having a number average molecular weight (Mn) in the range 750 to 6000, (b) a polyalphaolefin having a viscosity at 100° C.
  • A may represent any C 2-8 alkylene group, it is preferably derived from an alkylene oxide, and most preferably represents a 1,2-ethylene, 1,2-propylene or 1,2-butylene group.
  • R is preferably a linear group, and preferably represents a singly or multiply-unsaturated C 15-19 alkenyl group, optionally substituted by one or more —OH groups.
  • the fatty acid from which the salt is derived may very conveniently be oleic acid, linoleic acid, linolenic acid, or a mixture of fatty acids containing any two or all three of such acids, e.g. tall oil fatty acid or rapeseed oil fatty acid.
  • Z preferably represents a polymethylene group of formula —(CH 2 )n—, where n is 2 to 8, more preferably 2 to 6, either as single entities (e.g. an alpha, omega-alkylene group) or a mixture of alpha, omega-alkylene groups.
  • variable m preferably represents 1 or 2, more preferably 1.
  • the total of all variables x preferably has a value of 75% to 125% of (m+3).
  • the value of each x is most preferably 1.
  • each moiety A independently represents a 1,2-ethylene, 1,2-propylene or 1,2-butylene group, (most preferably a 1,2-propylene group) each moiety R independently represents a singly or multiply-unsaturated C 15-19 alkenyl group, optionally substituted by one or more —OH groups (R—COOH most preferably being oleic acid, linoleic acid or a mixture thereof), each moiety is a polymethylene group of formula —(CH 2 )n—, where n is 2 to 6, m is 1 or 2, and the total of all variables x has a value of 75% to 125% of (m+3) (most preferably each x being 1).
  • fatty acid salts of formula I may be synthesised as described in DE-A-19955651.
  • the nitrogen-containing detergent (a) containing a hydrocarbyl group having a number average molecular weight (Mn) in the range 750 to 6000 may be an amine, e.g. a polyisobutylene mono-amine or polyamine, such as a polyisobutylene ethylene diamine, or N-polyisobutenyl-N′,N′-dimethyl-1,3-diaminopropane, or amides, e.g. a polyisobutenyl succinimide, and are variously descsribed, for example, in U.S. Pat. No. 5,855,629 and WO 0132812.
  • a particularly preferred nitrogen-containing detergent is hydrocarbyl amine of formula R 1 —NH 2 and R 1 represents a group R 2 or a group R 2 —CH 2 — and R 2 represents a hydrocarbyl group having a number average molecular weight in the range 750 to 6000, preferably in the range 900 to 3000, more preferably 950 to 2000, and most preferably in the range 950 to 1350, e.g. a polybutenyl or polyisobutenyl group having a number average molecular weight in the range 950 to 1050.
  • the nitrogen-containing detergents (a) are known materials and may be prepared by known methods or by methods analogous to known methods.
  • U.S. Pat. No. 4,832,702 describes the preparation of polybutenyl and polyisobutenyl amines from an appropriate polybutene or polyisobutene by hydroformylation and subsequent amination of the resulting oxo product under hydrogenating conditions.
  • Suitable hydrocarbyl amines are obtainable from BASF A.G., under the trade mark “Kerocom”.
  • the polyalphaolefins (b) are primarily trimers, tetramers and pentamers, and synthesis of such materials is outlined in Campen et al. “Growing use of synlubes”, Hydrocarbon Processing, February 1982, Pages 75 to 82.
  • the polyalphaolefin may be unhydrotreated, but it is preferably a hydrogenated oligomer.
  • the polyalphaolefin (b) is preferably derived from an alphaolefinic monomer containing from 8 to 12 carbon atoms. Furthermore, it preferably has viscosity at 100° C. in the range 6 ⁇ 10 ⁇ 6 to 1 ⁇ 10 ⁇ 5 m 2 /s (6 to 10 centistokes).
  • Polyalphaolefins derived from decene-1 have been found to be very effective.
  • Polyalphaolefin having a viscosity at 100° C. of 8 ⁇ 10 ⁇ 6 m 2 /s (8 centistokes) has been found to be very effective.
  • the polyoxyalkylene compound (c) preferably has the formula II
  • R 3 and R 4 independently represent hydrogen atoms or hydrocarbyl, preferably C 1-40 hydrocarbyl, e.g. alkyl, cycloalkyl, phenyl or alkyl-phenyl groups
  • each R 5 independently represents an alkylene, preferably C 2-8 alkylene, group
  • p is such that Mn of the polyoxyalkylene compound is in the range 400 to 3000, preferably 700 to 2000, more preferably 1000 to 2000.
  • R 3 represents a C 8-20 alkyl group and R 4 represents a hydrogen atom.
  • R 3 preferably represents a C 8-18 alkyl group, more preferably a C 8-15 alkyl group.
  • R 3 may conveniently be a mixture of C 8-15 alkyl groups.
  • each group R 5 are preferably 1,2 alkylene groups.
  • each group R 5 independently represents a C 2-4 alkylene group, e.g. an ethylene, 1,2-propylene or 1,2-butylene group. Very effective results have been obtained when each group R 5 represents a 1,2-propylene group.
  • Number average molecular weights e.g. of hydrocarbons such as polyalkenes, may be determined by several techniques which give closely similar results. Conveniently Mn may be determined by vapour phase osmometry (VPO) (ASTM D 3592) or by modern gel permeation chromatography (GPC), e.g. as described for example in W. W. Yau, J. J. Kirkland and D. D. Bly, “Modern Size Exclusion Liquid Chromatography”, John Wiley and Sons, New York, 1979. Where the formula of a compound is known, the number average molecular weight can be calculated as its formula weight.
  • VPO vapour phase osmometry
  • GPC gel permeation chromatography
  • gasolines suitable for use in spark ignition engines are mixtures of hydrocarbons having boiling points in the range from 25° C. to 232° C. and comprising mixtures of saturated hydrocarbons, olefinic hydrocarbons and aromatic hydrocarbons.
  • Preferred are gasoline blends having a saturated hydrocarbon content ranging from 40 to 80 per cent volume, an olefinic hydrocarbon content ranging from 0 to 30 per cent volume and an aromatic hydrocarbon content ranging from 10 to 60 per cent volume.
  • the gasoline can be derived from straight run gasoline, polymer gasoline, natural gasoline, dimer- or trimerised olefins, synthetically produced aromatic hydrocarbon mixtures from thermally or catalytically reformed hydrocarbons, or from catalytically cracked or thermally cracked petroleum stocks, or mixtures thereof.
  • the hydrocarbon composition and octane level of the gasoline are not critical.
  • the octane level, (R+M)/2, will generally be above 85.
  • Any conventional gasoline can be used.
  • hydrocarbons can be replaced by up to substantial amounts of conventional alcohols or ethers conventionally known for use in gasoline.
  • the “gasoline” may consist essentially of ethanol.
  • the gasoline is preferably lead-free, and this may be required by law. Where permitted, lead-free antiknock compounds and/or valve-seat recession protectant compounds (e.g. known potassium salts, sodium salts or phosphorous compounds) may be present.
  • lead-free antiknock compounds and/or valve-seat recession protectant compounds e.g. known potassium salts, sodium salts or phosphorous compounds
  • Modern gasolines are inherently low-sulphur fuels, e.g. containing less than 200 ppmw sulphur.
  • the gasoline composition may additionally contain one or more corrosion inhibitors, anti-oxidants, dyes, dehazers, metal deactivators, detergents other than a nitrogen-containing detergent (a) (e.g. a polyether amine), carriers other than a polyalphaolefin (b) or a polyoxyalkylene compound (c), diluents and markers.
  • a nitrogen-containing detergent e.g. a polyether amine
  • b e.g. a polyalphaolefin
  • c polyoxyalkylene compound
  • the fatty acid salt is preferably present in an amount in the range 25 to 1000 ppmw, more preferably 25 to 400 ppmw. It is further preferred for the amount to be at least 50 ppmw. Amounts in the range 50 to 200 ppmw have been found to be very effective.
  • the co-additive is preferably present in an amount in the range 600 to 1500 ppmw, more preferably 700 to 1500 ppmw, conveniently 700 to 1200 ppmw, based on total composition.
  • the composition preferably contains at least 400 ppmw, based on total composition, of at least one of (b) and (c).
  • the composition may, for example, contain at least 200 ppmw of (b) and at least 200 ppmw of (c). Amounts of (b) and/or (c) individually in the range 200 to 800, subject to preferred overall maxima for concentration of co-additive are preferred.
  • a gasoline composition of the invention may contain 200 to 800 ppmw (b) and 200 to 800 ppmw (c), the ratio (b):(c) being in the range 4:1 to 1:4, preferably 3:1 to 1:3, subject to total concentration of (a) (where present), (b) and (c) being in the range 600 to 2000 ppmw, preferably 600 to 1500 ppmw, more preferably 700 to 1500, conveniently 700 to 1200 ppmw.
  • One example would be 200 ppmw of a polyalphaolefin (b) and 600 ppmw of a polyoxyalkylene compound (c).
  • amounts (concentrations) (ppmw) of fatty acid salt, of co-additive, and of individual components (a), (b) and (c) are of active matter, i.e. exclusive of volatile solvents/diluent materials.
  • the invention further provides a process for the preparation of a gasoline composition of the invention as defined above which comprises bringing into admixture the gasoline, the fatty acid salt and the co-additive.
  • the fatty acid salt, the co-additive, and any additional components such as corrosion inhibitors, anti-oxidants, etc., as listed above may be co-mixed, preferably together with suitable diluent(s), in an additive concentrate, and the additive concentrate may be dispersed into gasoline, in suitable quantity to result in a composition of the invention.
  • the invention also provides a method of operating a spark-ignition engine, which comprises bringing into the combustion chambers of said engine a gasoline composition of the invention as defined above.
  • base fuel used was an unleaded gasoline (95 USG) of RON 95.2, MON 87.2, and having sulphur content (ASTM D 2622-94) 12 ppmw, aromatics content (DIN 51413/T3) of 31.93 v/v, total paraffins content 61.56 v/v, density (DIN 51757/V4) 733.3 kg/m 3 , distillation (ISO 3405/88) IBP 38° C., 10% v/v 55° C., 50 % v/v 101° C., 90% v/v 142° C. and FBP 169° C.
  • FM this was a friction modifier additive in the form of a fatty acid salt of an alkoxylated oligoamine of general formula I
  • indices A represent 1,2-propylene groups
  • variables R represent a mixture of C 17 moieties such that R—COOH corresponds to a mixture of oleic and linoleic acids in approximate molar ratio 2:1
  • Z represents polymethylene groupings of formula —(CH 2 )n—, where n is 2 to 6, m is 1, and x is 1, prepared in analogous manner to Example 1 of DE-A-19953651 using a mixture of alpha, omega —C 2-6 diamines in place of ethylene diamine, and a 2:1 mixture of oleic and linoleic acids in place of oleic acid per se.
  • DP this was a standard commercial gasoline additive package, containing a polyisobutyleneamine detergent, a synthetic carrier oil and a conventional corrosion inhibitor, corresponding closely to additive package PI of Example 3 of DE-A-19955651.
  • the polyisobutyleneamine detergent was a polyisobutylene monoamine (PIBA) ex BASF, in which the polyisobutylene (PIB) chain has a number average molecular weight of approximately 1000.
  • the synthetic carrier oil was a polyether carrier fluid similar to PCF and PGHE below.
  • the additive package contained about 68% in non-volatile matter, about 27 % w of the package being the PIBA and 40 % w of the package being the polyether carrier fluid.
  • PCF is a polyether carrier fluid, similar to PGHE below and to the synthetic carrier oil in “DP” above, being a polyoxypropylene glycol hemiether containing 15 to 30 propylene oxide units prepared using a mixture of alkanols in the C 8-15 range as initiator (having Mn in the range 1000 to 2000).
  • PGHE polyether carrier fluid in the form of a polyoxypropylene glycol hemiether (monoether) prepared using a mixture of C 12-15 alcohols as initiator having Mn in the range 1200 to 1500 and a kinematic viscosity in the range 72 to 82 mm2/s at 40° C. according to ASTM D 445.
  • PGHE contains 17 to 22 propylene oxide units.
  • PAO this is a polyalphaolefin, being a hydrogenated oligomer of decene-1 having a viscosity at 100° C. of 8 ⁇ 10 ⁇ 6 m 2 /s (8 centistokes).
  • the test is based on a cycle of engine accelerations from 1300 to 4000 rpm as set forth in Table 1: TABLE 1 Engine Engine Throttle Coolant Oil Cycle Speed Torque StageTime position out in (temp. Stage (rpm) (Nm) (s) (%) (tem., ° C.) ° C.) 1 1300 20 7 13 100 105 2 1300- 140 Variable 100 100 105 4000 3 4000- 90 5 13 100 105 1300
  • Stage time for stage 2 is variable, according to the fuel used, being approximately 8 seconds for base fuel. Acceleration times are measured in Stage 2 for the time interval taken for the engine to pass from 1500 to 3500 rpm.
  • test fuel which comprises the same base fuel plus additive(s)
  • test fuel which comprises the same base fuel plus additive(s)
  • a sequence of 40 test cycles is made to establish an average test fuel acceleration time.
  • acceleration time benefit as a percentage of the difference between the acceleration times relative to the base fuel time.
  • Example 3 of DE-A-19955651 tests were effected on lubricity of gasolines, including gasolines containing zero additive, 500 mg/kg (ppmw) of additive package P1, and 50 mg/kg (ppmw) of friction modifier product
  • Example 1 of DE-A-19955651 plus 500 mg/kg (ppmw) of additive package P1 using a high frequency reciprocating rig (HFFR) test, in which the gasoline used was a 50% distillation residue of a standard Eurosuper gasoline.
  • HFFR high frequency reciprocating rig

Abstract

The invention provides a gasoline composition comprising a major amount of a gasoline suitable for use in a spark ignition engine; 5 to 1000 ppmw, based on total composition, of a fatty acid salt of an alkoxylated oligoamine of general formula I
Figure US20030159340A1-20030828-C00001
wherein each moiety A independently represents an alkylene group of 2 to 8 carbon atoms, each moiety R independently represents a C7-23 alkyl or singly or multiply-unsaturated C7 to C23 alkenyl group, optionally substituted by one or more —OH groups, each moiety Z independently represents a C1-8 alkylene group, a C3-8 cycloalkylene group, or a C6-12 arylene or arylalkylene group, m represents 0 or an integer in the range 1 to 5, and the total of all variables x has a value of 50% to 300% of (m+3); and 600 to 2000 ppmw, based on total composition, of a co-additive selected from the group consisting of (a) a nitrogen-containing detergent containing a hydrocarbyl group having a number average molecular weight (Mn) in the range 750 to 6000, (b) a polyalphaolefin having a viscosity at 100° C. in the range 2×10−6 to 2×10 −5 m2/s (2 to 20 centistokes), being an oligomer containing 18 to 80 carbon atoms derived from at least one alphaolefinic monomer containing from 8 to 16 carbon atoms; (c) a polyoxyalkylene compound selected from glycols, mono- and diethers thereof, having number average molecular weight (Mn) in the range 400 to 3000; and mixtures of any two or all three of (a), (b) and (c).

Description

    FIELD OF THE INVENTION
  • This invention relates to gasoline compositions, more particularly to such compositions containing a fatty acid salt of an alkoxylated oligoamine, and their preparation. [0001]
  • BACKGROUND OF THE INVENTION
  • U.S. Pat. No. 4,131,583 discloses certain fatty acid salts of alkoxylated oligoamines and their use as corrosion inhibitors in aqueous coating agents for metal surfaces. [0002]
  • DE-A-19955651 (BASF) discloses the use of fatty acid salts of alkoxylated oligoamines of general formula I [0003]
    Figure US20030159340A1-20030828-C00002
  • wherein each moiety A independently represents an alkylene group of 2 to 8 carbon atoms, each moiety R independently represents a C[0004] 7-23 alkyl or singly or multiply-unsaturated C7 to C23 alkenyl group, optionally substituted by one or more —OH groups, each moiety Z independently represents a C1-8 alkylene group, a C3-8 cycloalkylene group or a C6-12 arylene or arylalkylene group, m represents 0 or an integer in the range 1 to 5, and the total of all variables x has a value of 50% to 300% of (m+3), as lubricity improvers for mineral oil products, including fuels and lubricating oils. Use in gasoline and in diesel fuels are specifically disclosed. Use is particularly described together with a polyisobutylene amine detergent and a polyether carrier oil therefor, and Example 3 in DE-A-19955651 specifically describes the advantageous lubricity properties of a composition based on a 50% distillation residue of a standard Eurosuper gasoline into which was incorporated 50 mg/kg (ppmw) of a specific salt of formula I and 500 mg/kg (ppmw) of an additive package containing a polyisobutylene amine detergent, a synthetic carrier oil and a conventional corrosion inhibitor. These lubricity properties are demonstrated in a high frequency reciprocating rig (HFFR) test.
  • DESCRIPTION OF THE INVENTION
  • It has now surprisingly been found that if a fatty acid salt of formula I is incorporated in a gasoline composition together with higher concentrations of certain co-additives than are disclosed in DE-A-19955651, significantly enhanced acceleration performance can be achieved from a spark-ignition engine fuelled by the gasoline composition. [0005]
  • DETAILED DESCRIPTION OF THE INVENTION
  • According to the present invention therefore, there is provided a gasoline composition comprising a major amount of a gasoline suitable for use in a spark ignition engine; 5 to 1000 ppmw, based on total composition, of a fatty acid salt of an alkoxylated oligoamine of general formula I [0006]
    Figure US20030159340A1-20030828-C00003
  • wherein each moiety A independently represents an alkylene group of 2 to 8 carbon atoms, each moiety R independently represents a C[0007] 7-23 alkyl or singly or multiply-unsaturated C7 to C23 alkenyl group, optionally substituted by one or more —OH groups, each moiety Z independently represents a C1-8 alkylene group, a C3-8 cycloalkylene group, or a C6-12 arylene or arylalkylene group, m represents 0 or an integer in the range 1 to 5, and the total of all variables x has a value of 50% to 300% of (m+3); and 600 to 2000 ppmw, based on total composition, of a co-additive selected from the group consisting of (a) a nitrogen-containing detergent containing a hydrocarbyl group having a number average molecular weight (Mn) in the range 750 to 6000, (b) a polyalphaolefin having a viscosity at 100° C. in the range 2×10−6 to 2×10−5 m2/s (2 to 20 centistokes), being an oligomer containing 18 to 80 carbon atoms derived from at least one alphaolefinic monomer containing from 8 to 16 carbon atoms; (c) a polyoxyalkylene compound selected from glycols, mono- and diethers thereof, having number average molecular weight (Mn) in the range 400 to 3000; and mixtures of any two or all three of (a), (b) and (c).
  • In formula I, although A may represent any C[0008] 2-8 alkylene group, it is preferably derived from an alkylene oxide, and most preferably represents a 1,2-ethylene, 1,2-propylene or 1,2-butylene group.
  • R is preferably a linear group, and preferably represents a singly or multiply-unsaturated C[0009] 15-19 alkenyl group, optionally substituted by one or more —OH groups. The fatty acid from which the salt is derived may very conveniently be oleic acid, linoleic acid, linolenic acid, or a mixture of fatty acids containing any two or all three of such acids, e.g. tall oil fatty acid or rapeseed oil fatty acid.
  • Z preferably represents a polymethylene group of formula —(CH[0010] 2)n—, where n is 2 to 8, more preferably 2 to 6, either as single entities (e.g. an alpha, omega-alkylene group) or a mixture of alpha, omega-alkylene groups.
  • The variable m preferably represents 1 or 2, more preferably 1. [0011]
  • The total of all variables x preferably has a value of 75% to 125% of (m+3). The value of each x is most preferably 1. [0012]
  • Accordingly, in formula I, it is preferred that each moiety A independently represents a 1,2-ethylene, 1,2-propylene or 1,2-butylene group, (most preferably a 1,2-propylene group) each moiety R independently represents a singly or multiply-unsaturated C[0013] 15-19 alkenyl group, optionally substituted by one or more —OH groups (R—COOH most preferably being oleic acid, linoleic acid or a mixture thereof), each moiety is a polymethylene group of formula —(CH2)n—, where n is 2 to 6, m is 1 or 2, and the total of all variables x has a value of 75% to 125% of (m+3) (most preferably each x being 1).
  • The fatty acid salts of formula I may be synthesised as described in DE-A-19955651. [0014]
  • The nitrogen-containing detergent (a) containing a hydrocarbyl group having a number average molecular weight (Mn) in the range 750 to 6000 may be an amine, e.g. a polyisobutylene mono-amine or polyamine, such as a polyisobutylene ethylene diamine, or N-polyisobutenyl-N′,N′-dimethyl-1,3-diaminopropane, or amides, e.g. a polyisobutenyl succinimide, and are variously descsribed, for example, in U.S. Pat. No. 5,855,629 and WO 0132812. [0015]
  • A particularly preferred nitrogen-containing detergent is hydrocarbyl amine of formula R[0016] 1—NH2 and R1 represents a group R2 or a group R2—CH2— and R2 represents a hydrocarbyl group having a number average molecular weight in the range 750 to 6000, preferably in the range 900 to 3000, more preferably 950 to 2000, and most preferably in the range 950 to 1350, e.g. a polybutenyl or polyisobutenyl group having a number average molecular weight in the range 950 to 1050.
  • The nitrogen-containing detergents (a) are known materials and may be prepared by known methods or by methods analogous to known methods. For example, U.S. Pat. No. 4,832,702 describes the preparation of polybutenyl and polyisobutenyl amines from an appropriate polybutene or polyisobutene by hydroformylation and subsequent amination of the resulting oxo product under hydrogenating conditions. [0017]
  • Suitable hydrocarbyl amines are obtainable from BASF A.G., under the trade mark “Kerocom”. [0018]
  • The polyalphaolefins (b) are primarily trimers, tetramers and pentamers, and synthesis of such materials is outlined in Campen et al. “Growing use of synlubes”, Hydrocarbon Processing, February 1982, Pages 75 to 82. The polyalphaolefin may be unhydrotreated, but it is preferably a hydrogenated oligomer. The polyalphaolefin (b) is preferably derived from an alphaolefinic monomer containing from 8 to 12 carbon atoms. Furthermore, it preferably has viscosity at 100° C. in the range 6×10[0019] −6 to 1×10−5 m2/s (6 to 10 centistokes). Polyalphaolefins derived from decene-1 have been found to be very effective. Polyalphaolefin having a viscosity at 100° C. of 8×10−6 m2/s (8 centistokes) has been found to be very effective.
  • The polyoxyalkylene compound (c) preferably has the formula II [0020]
    Figure US20030159340A1-20030828-C00004
  • wherein R[0021] 3 and R4 independently represent hydrogen atoms or hydrocarbyl, preferably C1-40 hydrocarbyl, e.g. alkyl, cycloalkyl, phenyl or alkyl-phenyl groups, each R5 independently represents an alkylene, preferably C2-8 alkylene, group, and p is such that Mn of the polyoxyalkylene compound is in the range 400 to 3000, preferably 700 to 2000, more preferably 1000 to 2000.
  • Preferably R[0022] 3 represents a C8-20 alkyl group and R4 represents a hydrogen atom. R3 preferably represents a C8-18 alkyl group, more preferably a C8-15 alkyl group. R3 may conveniently be a mixture of C8-15 alkyl groups.
  • In the formula II the groups R[0023] 5 are preferably 1,2 alkylene groups. Preferably each group R5 independently represents a C2-4 alkylene group, e.g. an ethylene, 1,2-propylene or 1,2-butylene group. Very effective results have been obtained when each group R5 represents a 1,2-propylene group.
  • Number average molecular weights, e.g. of hydrocarbons such as polyalkenes, may be determined by several techniques which give closely similar results. Conveniently Mn may be determined by vapour phase osmometry (VPO) (ASTM D 3592) or by modern gel permeation chromatography (GPC), e.g. as described for example in W. W. Yau, J. J. Kirkland and D. D. Bly, “Modern Size Exclusion Liquid Chromatography”, John Wiley and Sons, New York, 1979. Where the formula of a compound is known, the number average molecular weight can be calculated as its formula weight. [0024]
  • Typical of gasolines suitable for use in spark ignition engines are mixtures of hydrocarbons having boiling points in the range from 25° C. to 232° C. and comprising mixtures of saturated hydrocarbons, olefinic hydrocarbons and aromatic hydrocarbons. Preferred are gasoline blends having a saturated hydrocarbon content ranging from 40 to 80 per cent volume, an olefinic hydrocarbon content ranging from 0 to 30 per cent volume and an aromatic hydrocarbon content ranging from 10 to 60 per cent volume. The gasoline can be derived from straight run gasoline, polymer gasoline, natural gasoline, dimer- or trimerised olefins, synthetically produced aromatic hydrocarbon mixtures from thermally or catalytically reformed hydrocarbons, or from catalytically cracked or thermally cracked petroleum stocks, or mixtures thereof. The hydrocarbon composition and octane level of the gasoline are not critical. The octane level, (R+M)/2, will generally be above 85. Any conventional gasoline can be used. For example, in the gasoline, hydrocarbons can be replaced by up to substantial amounts of conventional alcohols or ethers conventionally known for use in gasoline. Alternatively, e.g. in countries such as Brazil, the “gasoline” may consist essentially of ethanol. [0025]
  • The gasoline is preferably lead-free, and this may be required by law. Where permitted, lead-free antiknock compounds and/or valve-seat recession protectant compounds (e.g. known potassium salts, sodium salts or phosphorous compounds) may be present. [0026]
  • Modern gasolines are inherently low-sulphur fuels, e.g. containing less than 200 ppmw sulphur. [0027]
  • In addition to the fatty acid salt of formula I and the co-additive, the gasoline composition may additionally contain one or more corrosion inhibitors, anti-oxidants, dyes, dehazers, metal deactivators, detergents other than a nitrogen-containing detergent (a) (e.g. a polyether amine), carriers other than a polyalphaolefin (b) or a polyoxyalkylene compound (c), diluents and markers. [0028]
  • In gasoline compositions of the present invention, the fatty acid salt is preferably present in an amount in the range 25 to 1000 ppmw, more preferably 25 to 400 ppmw. It is further preferred for the amount to be at least 50 ppmw. Amounts in the range 50 to 200 ppmw have been found to be very effective. [0029]
  • The co-additive is preferably present in an amount in the range 600 to 1500 ppmw, more preferably 700 to 1500 ppmw, conveniently 700 to 1200 ppmw, based on total composition. [0030]
  • The composition preferably contains at least 400 ppmw, based on total composition, of at least one of (b) and (c). The composition may, for example, contain at least 200 ppmw of (b) and at least 200 ppmw of (c). Amounts of (b) and/or (c) individually in the range 200 to 800, subject to preferred overall maxima for concentration of co-additive are preferred. [0031]
  • For example, a gasoline composition of the invention may contain 200 to 800 ppmw (b) and 200 to 800 ppmw (c), the ratio (b):(c) being in the range 4:1 to 1:4, preferably 3:1 to 1:3, subject to total concentration of (a) (where present), (b) and (c) being in the range 600 to 2000 ppmw, preferably 600 to 1500 ppmw, more preferably 700 to 1500, conveniently 700 to 1200 ppmw. One example, would be 200 ppmw of a polyalphaolefin (b) and 600 ppmw of a polyoxyalkylene compound (c). [0032]
  • In this specification, amounts (concentrations) (ppmw) of fatty acid salt, of co-additive, and of individual components (a), (b) and (c) are of active matter, i.e. exclusive of volatile solvents/diluent materials. [0033]
  • The invention further provides a process for the preparation of a gasoline composition of the invention as defined above which comprises bringing into admixture the gasoline, the fatty acid salt and the co-additive. [0034]
  • If desired, the fatty acid salt, the co-additive, and any additional components such as corrosion inhibitors, anti-oxidants, etc., as listed above, may be co-mixed, preferably together with suitable diluent(s), in an additive concentrate, and the additive concentrate may be dispersed into gasoline, in suitable quantity to result in a composition of the invention. [0035]
  • The invention also provides a method of operating a spark-ignition engine, which comprises bringing into the combustion chambers of said engine a gasoline composition of the invention as defined above.[0036]
  • The invention will be further understood from the following illustrative examples, in which, unless otherwise indicated, parts and percentages are by weight, and the temperatures are in degrees Celsius. [0037]
  • In the examples, base fuel used was an unleaded gasoline (95 USG) of RON 95.2, MON 87.2, and having sulphur content (ASTM D 2622-94) 12 ppmw, aromatics content (DIN 51413/T3) of 31.93 v/v, total paraffins content 61.56 v/v, density (DIN 51757/V4) 733.3 kg/m[0038] 3, distillation (ISO 3405/88) IBP 38° C., 10% v/v 55° C., 50 % v/v 101° C., 90% v/v 142° C. and FBP 169° C.
  • Fuels were blended with additives by adding additives to base fuel at ambient temperature and homogenising. [0039]
  • The following additives were used: [0040]
  • “FM”—this was a friction modifier additive in the form of a fatty acid salt of an alkoxylated oligoamine of general formula I [0041]
    Figure US20030159340A1-20030828-C00005
  • wherein indices A represent 1,2-propylene groups, variables R represent a mixture of C[0042] 17 moieties such that R—COOH corresponds to a mixture of oleic and linoleic acids in approximate molar ratio 2:1, Z represents polymethylene groupings of formula —(CH2)n—, where n is 2 to 6, m is 1, and x is 1, prepared in analogous manner to Example 1 of DE-A-19953651 using a mixture of alpha, omega —C2-6 diamines in place of ethylene diamine, and a 2:1 mixture of oleic and linoleic acids in place of oleic acid per se.
  • “DP”—this was a standard commercial gasoline additive package, containing a polyisobutyleneamine detergent, a synthetic carrier oil and a conventional corrosion inhibitor, corresponding closely to additive package PI of Example 3 of DE-A-19955651. The polyisobutyleneamine detergent was a polyisobutylene monoamine (PIBA) ex BASF, in which the polyisobutylene (PIB) chain has a number average molecular weight of approximately 1000. The synthetic carrier oil was a polyether carrier fluid similar to PCF and PGHE below. The additive package contained about 68% in non-volatile matter, about 27 % w of the package being the PIBA and 40 % w of the package being the polyether carrier fluid. [0043]
  • “PCF”—this is a polyether carrier fluid, similar to PGHE below and to the synthetic carrier oil in “DP” above, being a polyoxypropylene glycol hemiether containing 15 to 30 propylene oxide units prepared using a mixture of alkanols in the C[0044] 8-15 range as initiator (having Mn in the range 1000 to 2000).
  • “PGHE”—this is a polyether carrier fluid in the form of a polyoxypropylene glycol hemiether (monoether) prepared using a mixture of C[0045] 12-15 alcohols as initiator having Mn in the range 1200 to 1500 and a kinematic viscosity in the range 72 to 82 mm2/s at 40° C. according to ASTM D 445. “PGHE” contains 17 to 22 propylene oxide units.
  • “PAO”—this is a polyalphaolefin, being a hydrogenated oligomer of decene-1 having a viscosity at 100° C. of 8×10[0046] −6 m2/s (8 centistokes).
  • “DET”—this is a 50 %w solution in volatile hydrocarbon solvent of the PIBA component of DP above. [0047]
  • Fuels were tested for acceleration performance using a Ford Zetec 2.0 litre in-line 4 cylinder, 16-valve, multipoint fuel injection, spark-ignition engine, in a bench engine test as follows. [0048]
  • The test is based on a cycle of engine accelerations from 1300 to 4000 rpm as set forth in Table 1: [0049]
    TABLE 1
    Engine Engine Throttle Coolant Oil
    Cycle Speed Torque StageTime position out in (temp.
    Stage (rpm) (Nm) (s) (%) (tem., ° C.) ° C.)
    1 1300 20 7 13 100 105
    2 1300- 140 Variable 100 100 105
    4000
    3 4000- 90 5 13 100 105
    1300
  • Stage time for stage 2 is variable, according to the fuel used, being approximately 8 seconds for base fuel. Acceleration times are measured in Stage 2 for the time interval taken for the engine to pass from 1500 to 3500 rpm. [0050]
  • In the test, a sequence of 40 test cycles is made to establish an average base fuel acceleration time. The fuel is then changed to test fuel (which comprises the same base fuel plus additive(s)), and a sequence of 40 test cycles is made to establish an average test fuel acceleration time. For each test fuel, there is established an acceleration time benefit as a percentage of the difference between the acceleration times relative to the base fuel time. [0051]
  • Following a test as described above, a purging procedure is carried out, in which the engine is run for 16 hours on base fuel, with three engine oil changes being carried out during that period, in order to ensure that there is no contamination of engine oil by test fuel additives in subsequent tests. [0052]
  • Details of the test fuels and acceleration performance data are given in Table 2 following, wherein Examples 1 to 5 are examples of the invention, and Comp. A to Comp. E are comparative examples: [0053]
    TABLE 2
    Additive Acceleration
    FM Additive active performance
    dose dose matter benefit
    Example (ppmw) Additive (ppmw) (ppmw) (%)
    1 50 DP 1680 1126* 3.090
    2 100 DP 1680 1126* 2.753
    3 200 DP 1680 1126* 3.840
    4 50 PAO 800  800 2.437
    5 50 PCF 800  800 2.935
    Comp. A 50 DP 525  352** 1.950
    Comp. B 800 1.577
    Comp. C PIBA 907  454 0.695
    Comp. D PGHE 672  672 1.91
    Comp. E DP 1680 1126* 2.13
  • In Example 3 of DE-A-19955651, tests were effected on lubricity of gasolines, including gasolines containing zero additive, 500 mg/kg (ppmw) of additive package P1, and 50 mg/kg (ppmw) of friction modifier product Example 1 of DE-A-19955651 plus 500 mg/kg (ppmw) of additive package P1, using a high frequency reciprocating rig (HFFR) test, in which the gasoline used was a 50% distillation residue of a standard Eurosuper gasoline. [0054]
  • Addition of PI alone (or the similar P2 package) was said to result in frictional wear values of the same order of magnitude as the blank values, whilst addition of 50 ppmw of the friction modifies product of Example 1 gave lower values, and results which were stated to be clearly superior to those resulting from inclusion of 50 ppmw of a prior art lubricity improver. [0055]
  • In the light of the teaching of Example 3 of DE-A-19955651, the acceleration performance findings of the present invention as evidenced by Table 2 above are extremely surprising. In particular, it should be noted that the comparative example Comp. A corresponds very closely to the combination giving the best results in Example 3 of DE-A-19955651. [0056]

Claims (10)

What is claimed is:
1. A gasoline composition comprising a major amount of a gasoline suitable for use in a spark ignition engine; 5 to 1000 ppmw, based on total composition, of a fatty acid salt of an alkoxylated oligoamine of general formula I
Figure US20030159340A1-20030828-C00006
wherein each moiety A independently represents an alkylene group of 2 to 8 carbon atoms, each moiety R independently represents a C7-23 alkyl or singly or multiply-unsaturated C7 to C23 alkenyl group, optionally substituted by one or more —OH groups, each moiety Z independently represents a C1-8 alkylene group, a C3-8 cycloalkylene group, or a C6-12 arylene or arylalkylene group, m represents 0 or an integer in the range 1 to 5, and the total of all variables x has a value of 50% to 300% of (m+3); and 600 to 2000 ppmw, based on total composition, of a co-additive selected from the group consisting of (a) a nitrogen-containing detergent containing a hydrocarbyl group having a number average molecular weight (Mn) in the range 750 to 6000, (b) a polyalphaolefin having a viscosity at 100° C. in the range 2×10−6 to 2×10−5 m2/s (2 to 20 centistokes), being an oligomer containing 18 to 80 carbon atoms derived from at least one alphaolefinic monomer containing from 8 to 16 carbon atoms; (c) a polyoxyalkylene compound selected from glycols, mono- and diethers thereof, having number average molecular weight (Mn) in the range 400 to 3000; and mixtures of any two or all three of (a), (b) and (c).
2. The composition according to claim 1 wherein in formula I each moiety A independently represents a 1,2-ethylene, ethylene, 1,2-propylene or 1,2-butylene group, each moiety R independently represents a singly or multiply-unsaturated C15-19 alkenyl group, optionally substituted by one or more —OH groups, each moiety Z is a polymethylene group of formula —(CH2)n—, where n is 2 to 6, m is 1 or 2, and the total of all variables x has a value of 75% to 125% of (m+3).
3. The composition according to claim 1 wherein the nitrogen-containing detergent (a) is a hydrocarbyl amine or formula R1—NH2, wherein R1 represents a group R2 or a group R2—CH2—and R2 is a hydrocarbyl group having a number average molecular weight in the range 950 to 1350.
4. The composition according to claim 1, wherein the poyalphaolefin (b) is derived from an alphaolefinic monomer containing from 8 to 12 carbon atoms, and has viscosity at 100° C. in the range 6×10−6 to 1×10−5 m2/s (6 to 10 centistokes).
5. The composition according to claim 1 wherein the polyoxyalkylene compound (c) has the formula II
Figure US20030159340A1-20030828-C00007
wherein R3 and R4 independently represent hydrogen atoms or C1-40 hydrocarbyl groups, each R5 independently represents a C2-8 alkylene group and n is such that M2 of the polyoxyalkylene compound is in the range 700 to 2000.
6. The composition according to claim 1, wherein the fatty acid salt is present in an amount in the range 25 to 400 ppmw, based on total composition.
7. The composition according to claim 1, wherein the co-additive is present in an amount in the range 700 to 1500 ppmw, based on total composition.
8. The composition according to claim 1 which contains at least 400 ppmw, based on total composition, of (b) and/or (c).
9. A process for the preparation of a gasoline composition according to claim 1 which comprises bringing into admixture the gasoline, the fatty acid salt and the co-additive.
10. A method of operating a spark-ignition internal combustion engine, which comprises bringing into the combustion chambers of said engine a gasoline composition according to claim 1.
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US7435272B2 (en) * 2002-04-24 2008-10-14 Afton Chemical Intangibles Friction modifier alkoxyamine salts of carboxylic acids as additives for fuel compositions and methods of use thereof
US7846224B2 (en) 2002-04-24 2010-12-07 Afton Chemical Intangibles, Llc Methods to improve the low temperature compatibility of amide friction modifiers in fuels and amide friction modifiers
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