US20100024286A1 - Liquid fuel compositions - Google Patents

Liquid fuel compositions Download PDF

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Publication number
US20100024286A1
US20100024286A1 US12/511,695 US51169509A US2010024286A1 US 20100024286 A1 US20100024286 A1 US 20100024286A1 US 51169509 A US51169509 A US 51169509A US 2010024286 A1 US2010024286 A1 US 2010024286A1
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liquid fuel
fuel composition
poly
hydroxycarboxylic acid
ppmw
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US12/511,695
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Susan Jane SMITH
Mark Clift SOUTHBY
Nigel Peter Tait
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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: SMITH, SUSAN JANE, SOUTHBY, MARK CLIFT, TAIT, NIGEL PETER
Publication of US20100024286A1 publication Critical patent/US20100024286A1/en
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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
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/238Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/2381Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds polyamides; polyamide-esters; polyurethane, polyureas
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    • 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
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    • 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
    • C10L1/224Amides; Imides carboxylic acid amides, imides
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    • 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
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    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2462Organic compounds containing sulfur, selenium and/or tellurium macromolecular compounds
    • C10L1/2475Organic compounds containing sulfur, selenium and/or tellurium macromolecular compounds obtained otherwise than by reactions only involving unsaturated carbon to carbon bonds
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    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/02Use of additives to fuels or fires for particular purposes for reducing smoke development
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    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/04Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
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    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/08Use of additives to fuels or fires for particular purposes for improving lubricity; for reducing wear
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/68Polyesters containing atoms other than carbon, hydrogen and oxygen
    • C08G63/685Polyesters containing atoms other than carbon, hydrogen and oxygen containing nitrogen
    • C08G63/6852Polyesters containing atoms other than carbon, hydrogen and oxygen containing nitrogen derived from hydroxy carboxylic acids
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G63/00Macromolecular compounds obtained by reactions forming a carboxylic ester link in the main chain of the macromolecule
    • C08G63/91Polymers modified by chemical after-treatment
    • C08G63/912Polymers modified by chemical after-treatment derived from hydroxycarboxylic acids
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    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1233Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof
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    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1266Inorganic compounds nitrogen containing compounds, (e.g. NH3)
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    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1283Inorganic compounds phosphorus, arsenicum, antimonium containing compounds
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    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/182Organic compounds containing oxygen containing hydroxy groups; Salts thereof
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    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/182Organic compounds containing oxygen containing hydroxy groups; Salts thereof
    • C10L1/183Organic compounds containing oxygen containing hydroxy groups; Salts thereof at least one hydroxy group bound to an aromatic carbon atom
    • C10L1/1832Organic compounds containing oxygen containing hydroxy groups; Salts thereof at least one hydroxy group bound to an aromatic carbon atom mono-hydroxy
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    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/188Carboxylic acids; metal salts thereof
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    • 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
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    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/188Carboxylic acids; metal salts thereof
    • C10L1/189Carboxylic acids; metal salts thereof having at least one carboxyl group bound to an aromatic carbon atom
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    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2431Organic compounds containing sulfur, selenium and/or tellurium sulfur bond to oxygen, e.g. sulfones, sulfoxides
    • C10L1/2437Sulfonic acids; Derivatives thereof, e.g. sulfonamides, sulfosuccinic acid esters

Definitions

  • the present invention relates to liquid fuel compositions comprising a major portion of a base fuel suitable for use in an internal combustion engine, in particular liquid fuel compositions comprising a major portion of a base fuel suitable for use in an internal combustion engine and a hyperdispersant.
  • EP 0164817 A2 discloses a surfactant comprising a carboxylic acid ester or amide carrying a terminal strong acid group selected from carboxymethyl, sulphate, sulphonate, phosphate and phosphonate, suitable for stabilising dispersions of solids in organic liquids and oil/water emulsions.
  • a preferred species of the surfactant is a poly(hydroxyalkanecarboxylic acid) having the strong acid group attached, either directly or through a linking group, to a terminal hydroxy or carboxylic acid group. The use of such surfactants in fuels is not disclosed therein.
  • EP 0233684 A1 discloses an ester or polyester having (i) a terminal group containing at least two aliphatic carbon-carbon double bonds and (ii) an acidic or basic amino group which is suitable for use as a dispersant for solids in organic liquids. The use of such surfactants in fuels is not disclosed therein.
  • GB 2197312 A discloses oil soluble dispersant additives, wherein said dispersant additives are poly (C 5 -C 9 lactone) adducts which have been prepared by first reacting a C 5 -C 9 lactone with a polyamine, a polyol or an amino alcohol to form an intermediate adduct, whereafter the intermediate adduct is reacted with an aliphatic hydrocarbyl monocarboxylic or dicarboxylic acylating agent having from about 1 to about 165 total carbon atoms.
  • the use of the dispersant additives in lubricating oils and fuels is also disclosed in GB 2197312 A.
  • EP 0802255 A2 discloses hydroxyl group containing acylated nitrogen compounds which are useful as low chlorine containing additives for lubricating oils and normally liquid fuels and a process for preparing the compounds.
  • WO 00/34418 A1 discloses the use of poly(hydroxycarboxylic acid)amide or -ester derivatives in fuel compositions as a lubricity additive. It is also disclosed in WO 00/34418 A1 that the use of the poly(hydroxycarboxylic acid)amide or -ester derivatives disclosed therein may also result in attaining one or more of a number of effects such as inlet system cleanliness (intake valves, fuel injectors, carburetors), combustion chamber cleanliness (in each case either or both of keep clean and clean-up effects), anti-corrosion (including anti-rust) and reduction or elimination of valve-stick.
  • inlet system cleanliness intake valves, fuel injectors, carburetors
  • combustion chamber cleanliness in each case either or both of keep clean and clean-up effects
  • anti-corrosion including anti-rust
  • the present invention provides a liquid fuel composition comprising:
  • Y is hydrogen or an optionally substituted hydrocarbyl group
  • A is a divalent optionally substituted hydrocarbyl group
  • n is from 1 to 100
  • m is from 1 to 4
  • q is from 1 to 4
  • Z is an optionally substituted divalent bridging group which is attached to the carbonyl group through a nitrogen atom
  • r is 0 or 1
  • R + is an ammonium group
  • X q ⁇ is an anion.
  • the present invention further provides a method for preparing a liquid fuel composition of the present invention comprising admixing the one or more poly(hydroxycarboxylic acid) amide salt derivatives with a base fuel suitable for use in an internal combustion engine.
  • the present invention yet further provides a method of operating an internal combustion engine, which method involves introducing into a combustion chamber of the engine a liquid fuel composition according to the present invention
  • poly(hydroxycarboxylic acid) amide salt derivatives can also surprisingly provides benefits in terms of improving the lubricity of liquid fuel compositions incorporated them.
  • the liquid fuel composition of the present invention comprises a base fuel suitable for use in an internal combustion engine and one or more poly(hydroxycarboxylic acid) amide salt derivatives.
  • the base fuel suitable for use in an internal combustion engine is a gasoline or a diesel fuel, and therefore the liquid fuel composition of the present invention is typically a gasoline composition or a diesel fuel composition.
  • poly(hydroxycarboxylic acid) amide salt derivatives used in the present invention may also be referred to as hyperdispersants.
  • the one or more poly(hydroxycarboxylic acid) amide salt derivatives in the liquid fuel compositions of the present invention are poly(hydroxycarboxylic acid) amide salt derivatives having formula (III):
  • Y is hydrogen or optionally substituted hydrocarbyl group
  • A is a divalent optionally substituted hydrocarbyl group
  • n is from 1 to 100
  • m is from 1 to 4
  • q is from 1 to 4
  • Z is an optionally substituted divalent bridging group which is attached to the carbonyl group through a nitrogen atom
  • r is 0 or 1
  • R + is an ammonium group
  • X q ⁇ is an anion.
  • R + may be a primary, secondary, tertiary or quaternary ammonium group.
  • R + is preferably a quaternary ammonium group.
  • A is preferably a divalent straight chain or branched hydrocarbyl group as hereafter described for formulae (I) and (II) below.
  • A is preferably an optionally substituted aromatic, aliphatic or cycloaliphatic straight chain or branched divalent hydrocarbyl group. More preferably, A is an arylene, alkylene or alkenylene group, in particular an arylene, alkylene or alkenylene group containing in the range of from 4 to 25 carbon atoms, more preferably in the range of from 6 to 25 carbon atoms, more preferably in the range of from 8 to 24 carbon atoms, more preferably in the range of from 10 to 22 carbon atoms, and most preferably in the range of from 12 to 20 carbon atoms.
  • said compound of formula (III) there are at least 4 carbon atoms, more preferably at least 6 carbon atoms, and even more preferably in the range of from 8 to 14 carbon atoms connected directly between the carbonyl group and the oxygen atom derived from the hydroxyl group.
  • the optional substituents in the group A are preferably selected from hydroxy, halo or alkoxy groups, especially C 1-4 alkoxy groups.
  • n is in the range of from 1 to 100.
  • the lower limit of the range for n is 1, more preferably 2, even more preferably 3; preferably the upper limit of the range for n is 100, more preferably 60, more preferably 40, more preferably 20, and even more preferably 10 (i.e. n may be selected from any of the following ranges: from 1 to 100; from 2 to 100; from 3 to 100; from 1 to 60; from 2 to 60; from 3 to 60; from 1 to 40; from 2 to 40; from 3 to 40; from 1 to 20; from 2 to 20; from 3 to 20; from 1 to 10; from 2 to 10; and, from 3 to 10).
  • Y is preferably an optionally substituted hydrocarbyl group as hereinafter described for formula (I).
  • the optionally substituted hydrocarbyl group Y in formula (III) is preferably aryl, alkyl or alkenyl containing up to 50 carbon atoms, more preferably in the range of from 7 to 25 carbon atoms.
  • the optionally substituted hydrocarbyl group Y may be conveniently selected from heptyl, octyl, undecyl, lauryl, heptadecyl, heptadenyl, heptadecadienyl, stearyl, oleyl and linoleyl.
  • optionally substituted hydrocarbyl group Y in formula (III) herein include C 4-8 cycloalkyls such as cyclohexyl; polycycloalkyls such as polycyclic terpenyl groups which are derived from naturally occurring acids such as abietic acid; aryls such as phenyl; aralkyls such as benzyl; and polyaryls such as naphthyl, biphenyl, stibenzyl and phenylmethylphenyl.
  • the optionally substituted hydrocarbyl group Y in formula (III) may contain one or more functional groups such as carbonyl, carboxyl, nitro, hydroxy, halo, alkoxy, amino, preferably tertiary amino (no N—H linkages), oxy, cyano, sulphonyl and sulphoxyl.
  • the majority of the atoms, other than hydrogen, in substituted hydrocarbyl groups are generally carbon, with the heteroatoms (e.g., oxygen, nitrogen and sulphur) generally representing only a minority, about 33% or less, of the total non-hydrogen atoms present.
  • the hydrocarbyl group Y in formula (III) is unsubstituted or substituted by a group selected from hydroxy, halo or alkoxy group, even more preferably C 1-4 alkoxy.
  • the optionally substituted hydrocarbyl group Y in formula (III) is a stearyl group, 12-hydroxystearyl group, an oleyl group or a 12-hydroxyoleyl group, and that derived from naturally occurring oil such as tall oil fatty acid.
  • Z is preferably an optionally substituted divalent bridging group represented by formula (IV)
  • R 1 is hydrogen or a hydrocarbyl group and B is an optionally substituted alkylene group.
  • hydrocarbyl groups that may represent R 1 include methyl, ethyl, n-propyl, n-butyl and octadecyl.
  • optionally substituted alkylene groups that may represent B include ethylene, trimethylene, tetramethylene and hexamethylene.
  • Examples of preferred Z moieties in formula (III) include —NHCH 2 CH 2 —, —NHCH 2 C(CH 3 ) 2 CH 2 — and —NH(CH 2 ) 3 —.
  • r is preferably 1, i.e. the poly(hydroxycarboxylic acid) amide salt derivative having formula (III) must contain the optionally substituted divalent bridging group Z.
  • R + may be represented by formula (V)
  • R 2 , R 3 and R 4 may be selected from hydrogen and alkyl groups such as methyl.
  • the anion X q ⁇ of the compound of formula (III) is not critical and can be any anion (or mixture of anions) suitable to balance the positive charge of the poly(hydroxycarboxylic acid) amide cation.
  • the anion X q ⁇ of the compound of formula (III) may conveniently be a sulphur-containing anion, such as an anion selected from sulphate and sulphonate anions.
  • non-sulphur-containing anions in the compounds of formula (III) may be desirable depending upon the concentration of sulphur in the liquid base fuel and/or the desired concentration of sulphur in the liquid fuel composition containing the one or more poly(hydroxycarboxylic acid) amide salt derivatives.
  • the anion X q ⁇ of the compound of formula (III) can also be any non-sulphur-containing anion (or mixture of anions) suitable to balance the positive charge of the poly(hydroxycarboxylic acid) amide cation, such as a non-sulphur-containing organic anion or a non-sulphur-containing inorganic anion.
  • Non-limiting examples of suitable anions are OH ⁇ , CH ⁇ , NH 3 ⁇ , HCO 3 ⁇ , HCOO ⁇ , CH 3 COO ⁇ , H ⁇ , BO 3 3 ⁇ , cO 3 2 ⁇ , C 2 H 3 O 2 ⁇ , HCO 2 ⁇ , C 2 O 4 2 ⁇ , HC 2 O 4 ⁇ , NO 2 ⁇ , NO 2 ⁇ , N 3 ⁇ , NH 2 ⁇ , O 2 ⁇ , O 2 2 ⁇ , BeF 3 ⁇ , F ⁇ , Na ⁇ , [Al(H 2 O) 2 (OH) 4 ] ⁇ , SiO 3 ⁇ , SiF 6 ⁇ , H 2 PO 4 ⁇ , P 3 ⁇ , PO 4 3 ⁇ , HPO 4 2 ⁇ , Cl ⁇ , ClO 3 ⁇ , ClO 4 ⁇ , ClO ⁇ , KO ⁇ , SbOH 6 ⁇ , SnC
  • Suitable anions may also include anions derived from compounds containing a carboxylic acid group (e.g. a carboxylate anion), anions derived from compounds containing a hydroxyl group (e.g. an alkoxide, phenoxide or enolate anion), nitrogen based anions such as nitrate and nitrite, phosphorus based anions such as phosphates and phosphonates, or mixtures thereof.
  • a carboxylic acid group e.g. a carboxylate anion
  • anions derived from compounds containing a hydroxyl group e.g. an alkoxide, phenoxide or enolate anion
  • nitrogen based anions such as nitrate and nitrite
  • phosphorus based anions such as phosphates and phosphonates, or mixtures thereof.
  • Non-limiting examples of suitable anions derived from compounds containing a carboxylic acid group include acetate, oleate, salicylate anions, and mixtures thereof.
  • Non-limiting examples of suitable anions derived from compounds containing a hydroxyl group include phenate anions, and mixtures thereof.
  • the anion X q ⁇ is a non-sulfur-containing anion selected from the group consisting of OH, a phenate group, a salicylate group, an oleate group and an acetate group; more preferably the anion X q ⁇ is OH.
  • the one or more poly(hydroxycarboxylic acid) amide salt derivatives may be obtained by reaction of an amine and a poly(hydroxycarboxylic acid) of formula (I)
  • Y is hydrogen or optionally substituted hydrocarbyl group
  • A is a divalent optionally substituted hydrocarbyl group
  • n is from 1 to 100, with an acid or a quaternizing agent.
  • hydrocarbyl represents a radical formed by removal of one or more hydrogen atoms from a carbon atom of a hydrocarbon (not necessarily the same carbon atoms in case more hydrogen atoms are removed).
  • Hydrocarbyl groups may be aromatic, aliphatic, acyclic or cyclic groups.
  • hydrocarbyl groups are aryl, cycloalkyl, alkyl or alkenyl, in which case they may be straight-chain or branched-chain groups.
  • Representative hydrocarbyl groups include phenyl, naphthyl, methyl, ethyl, butyl, pentyl, methylpentyl, hexenyl, dimethylhexyl, octenyl, cyclooctenyl, methylcyclooctenyl, dimethylcyclooctyl, ethylhexyl, octyl, isooctyl, dodecyl, hexadecenyl, eicosyl, hexacosyl, triacontyl and phenylethyl.
  • hydrocarbyl optionally substituted hydrocarbyl groups optionally containing one or more “inert” heteroatom-containing functional groups.
  • inert is meant that the functional groups do not interfere to any substantial degree with the function of the compound.
  • the optionally substituted hydrocarbyl group Y in formula (I) herein is preferably aryl, alkyl or alkenyl containing up to 50 carbon atoms, more preferably in the range of from 7 to 25 carbon atoms.
  • the optionally substituted hydrocarbyl group Y may be conveniently selected from heptyl, octyl, undecyl, lauryl, heptadecyl, heptadenyl, heptadecadienyl, stearyl, oleyl and linoleyl.
  • optionally substituted hydrocarbyl group Y in formula (I) herein include C 4-8 cycloalkyls such as cyclohexyl; polycycloalkyls such as polycyclic terpenyl groups which are derived from naturally occurring acids such as abietic acid; aryls such as phenyl; aralkyls such as benzyl; and polyaryls such as naphthyl, biphenyl, stibenzyl and phenylmethylphenyl.
  • the optionally substituted hydrocarbyl group Y may contain one or more functional groups such as carbonyl, carboxyl, nitro, hydroxy, halo, alkoxy, tertiary amino (no N—H linkages), oxy, cyano, sulphonyl and sulphoxyl.
  • the majority of the atoms, other than hydrogen, in substituted hydrocarbyl groups are generally carbon, with the heteroatoms (e.g., oxygen, nitrogen and sulphur) generally representing only a minority, about 33% or less, of the total non-hydrogen atoms present.
  • the hydrocarbyl group Y in formula (I) is more preferably unsubstituted or substituted by a group selected from hydroxy, halo or alkoxy group, even more preferably C 1-4 alkoxy.
  • the optionally substituted hydrocarbyl group Y in formula (I) is a stearyl group, 12-hydroxystearyl group, an oleyl group, a 12-hydroxyoleyl group or a group derived from naturally occurring oil such as tall oil fatty acid.
  • At least one of, or all of, the one or more poly(hydroxycarboxylic acid) amide salt derivatives are sulphur-containing poly(hydroxycarboxylic acid) amide salt derivatives.
  • said one or more poly(hydroxycarboxylic acid) amide salt derivatives preferably have a sulphur content of at most 2.5 wt. %, such as a sulphur content in the range of from 0.1 to 2.0 wt. %, conveniently in the range of from 0.6 to 1.2 wt. % sulphur, as measured by ICP-AES, based on the total weight of said poly(hydroxycarboxylic acid) amide salt derivatives.
  • the one or more poly(hydroxycarboxylic acid) amide salt derivatives are non-sulphur-containing poly(hydroxycarboxylic acid) amide salt derivatives.
  • poly(hydroxycarboxylic acid)s of formula (I) may be made by the interesterification of one or more hydroxycarboxylic acids of formula (II)
  • A is a divalent optionally substituted hydrocarbyl group, optionally in the presence of a catalyst according to well known methods. Such methods are described, for example, in U.S. Pat. No. 3,996,059, GB 1 373 660 and GB 1 342 746.
  • the chain terminator in said interesterification may be a non-hydroxycarboxylic acid.
  • the hydroxyl group in the hydroxycarboxylic acid and the carboxylic acid group in the hydroxycarboxylic acid or the non-hydroxycarboxylic acid may be primary, secondary or tertiary in character.
  • the interesterification of the hydroxycarboxylic acid and the non-hydroxycarboxylic acid chain terminator may be effected by heating the starting materials, optionally in a suitable hydrocarbon solvent such as toluene or xylene, and azeotroping off the formed water.
  • the reaction may be carried out at a temperature up to ⁇ 250° C., conveniently at the reflux temperature of the solvent.
  • the temperature employed should not be so high as to lead to dehydration of the acid molecule.
  • Catalysts for the interesterification such as p-toluenesulphonic acid, zinc acetate, zirconium naphthenate or tetrabutyl titanate, may be included, with the objective of either increasing the rate of reaction at a given temperature or of reducing the temperature required for a given rate of reaction.
  • A is preferably an optionally substituted aromatic, aliphatic or cycloaliphatic straight chain or branched divalent hydrocarbyl group.
  • A is an arylene, alkylene or alkenylene group, in particular an arylene, alkylene or alkenylene group containing in the range of from 4 to 25 carbon atoms, more preferably in the range of from 6 to 25 carbon atoms, more preferably in the range of from 8 to 24 carbon atoms, more preferably in the range of from 10 to 22 carbon atoms, and most preferably in the range of from 12 to 20 carbon atoms.
  • the optional substituents in the group A are preferably selected from hydroxy, halo or alkoxy groups, more preferably C 1-4 alkoxy groups.
  • the hydroxyl group in the hydroxycarboxylic acids of formula (II) is preferably a secondary hydroxyl group.
  • Suitable hydroxycarboxylic acids are 9-hydroxystearic acid, 10-hydroxystearic acid, 12-hydroxystearic acid, 12-hydroxy-9-oleic acid (ricinoleic acid), 6-hydroxycaproic acid, preferably 12-hydroxystearic acid.
  • Commercial 12-hydroxystearic acid hydrogenated castor oil fatty acid normally contains up to 15% wt of stearic acid and other non-hydroxycarboxylic acids as impurities and can conveniently be used without further admixture to produce a polymer of molecular weight about 1000-2000.
  • the proportion which is required in order to produce a polymer or oligomer of a given molecular weight can be determined either by simple experiment or by calculation by the person skilled in the art.
  • the group (—O-A-CO—) in the compounds of formulae (I) and (II) is preferably a 12-oxystearyl group, 12-oxyoleyl group or a 6-oxycaproyl group.
  • Preferred poly(hydroxycarboxylic acid)s of formula (I) for reaction with amine include poly(hydroxystearic acid) and poly(hydroxyoleic acid).
  • the amines which react with poly(hydroxycarboxylic acid)s of formula (I) to form poly(hydroxycarboxylic acid) amide intermediates may include those defined in WO 97/41092.
  • the amine reactant is preferably a diamine, a triamine or a polyamine.
  • Preferred amine reactants are diamines selected from ethylenediamine, N,N-dimethyl-1,3-propanediamine, triamines and polyamines selected from dietheylenetriamine, triethylenetetramine, tetraethylenepentamine, pentaethylenehexamine and tris(2-aminoethyl)amine.
  • the amidation between the amine reactant and the (poly(hydroxycarboxylic acid) of formula (I) may be carried out according to methods known to those skilled in the art, by heating the poly(hydroxycarboxylic acid) with the amine reactant, optionally in a suitable hydrocarbon solvent such as toluene or xylene, and azeotroping off the formed water. Said reaction may be carried out in the presence of a catalyst such as p-toluenesulphonic acid, zinc acetate, zirconium naphthenate or tetrabutyl titanate.
  • a catalyst such as p-toluenesulphonic acid, zinc acetate, zirconium naphthenate or tetrabutyl titanate.
  • GB 1 373 660 discloses poly(hydroxycarboxylic acid) amide derivatives with amines such as 3-dimethylaminopropylamine and ethylenediamine for use as dispersing agents in dispersions of pigments in organic liquids.
  • GB 2 001 083 discloses poly(hydroxycarboxylic acid) amide derivatives with poly(ethyleneimine) (PEI) having a molecular weight (MW) greater than 500 for a similar use.
  • PEI poly(ethyleneimine)
  • WO 95/17473 discloses poly(hydroxycarboxylic acid) amide derivatives with amines such as 3-dimethylaminopropylamine, ethylenediamine, poly(ethyleneimine) (PEI) having a molecular weight (MW) greater than 500 and amines of the formula of NH 2 R′—N(R′′)—R′′′—NH 2 for use in a method of preparing a non-aqueous dispersion of copper phthalocyanine.
  • amines such as 3-dimethylaminopropylamine, ethylenediamine, poly(ethyleneimine) (PEI) having a molecular weight (MW) greater than 500 and amines of the formula of NH 2 R′—N(R′′)—R′′′—NH 2 for use in a method of preparing a non-aqueous dispersion of copper phthalocyanine.
  • U.S. Pat. No. 4,349,389 discloses poly(hydroxycarboxylic acid) amide derivatives with amines such as 3-dimethyl-aminopropylamine, poly(ethyleneimine) (PEI) having a molecular weight (MW) greater than 500 as dispersing agent in the preparation of a dispersible inorganic pigment composition.
  • PEI poly(ethyleneimine)
  • EP 0 164 817 discloses poly(hydroxycarboxylic acid) amide derivatives with polyamines (ethylenediamine, diethylenetriamine, etc.), aminoalcohols (diethanolamine, etc.) and ester derivatives with polyols (glycerol, etc.) for use as surfactant suitable for stabilising dispersions of solids in organic liquids and oil/water emulsions.
  • the poly(hydroxycarboxylic acid) amide intermediate formed from reaction of the amine and the poly(hydroxycarboxylic acid) of formula (I) is reacted with an acid or a quaternizing agent to form a salt derivative, according to well-known methods.
  • Acids that may be used to form the salt derivative may be selected from organic or inorganic acids.
  • Said acids are conveniently selected from carboxylic acids, nitrogen-containing organic and inorganic acids, sulphur-containing organic or inorganic acids (such as sulphuric acid, methanesulphonic acid and benzenesulphonic acid).
  • Quaternizing agents that may be used to form the salt derivative may be selected from dimethylsulphuric acid, a dialkyl sulphate having from 1 to 4 carbon atoms, an alkyl halide such as methyl chloride, methyl bromide, aryl halide such as benzyl chloride.
  • the quaternizing agent is a sulphur-containing quaternizing agent, in particular dimethylsulphuric acid or an dialkyl sulphate having from 1 to 4 carbon atoms.
  • the quaternizing agent is preferably dimethyl sulphate.
  • Quaternization is a well-known method in the art. For example, quaternization using dimethyl sulphate is described in U.S. Pat. No. 3,996,059, U.S. Pat. No. 4,349,389 and GB 1 373 660.
  • Poly(hydroxycarboxylic acid) amide salt derivatives that are preferred in the present invention are those which each have a TBN (total base number) value of less than 10 mg ⁇ KOH/g, as measured by ASTM D 4739. More preferably, the poly(hydroxycarboxylic acid) amide salt derivatives each have a TBN value of less than 5 mg ⁇ KOH/g, most preferably 2 mg ⁇ KOH/g or less, as measured by ASTM D 4739.
  • poly(hydroxycarboxylic acid) amide salt derivatives that are available commercially include that available from Lubrizol under the trade designation “SOLSPERSE 17000” (a reaction product of poly(12-hydroxystearic acid) with N,N-dimethyl-1,3-propanediamine and dimethyl sulphate) and those available under the trade designations “CH-5” and “CH-7” from Shanghai Sanzheng Polymer Company.
  • SOLSPERSE 17000 a reaction product of poly(12-hydroxystearic acid) with N,N-dimethyl-1,3-propanediamine and dimethyl sulphate
  • the base fuel used is a gasoline
  • the gasoline may be any gasoline suitable for use in an internal combustion engine of the spark-ignition (petrol) type known in the art.
  • the gasoline used as the base fuel in the liquid fuel composition of the present invention may conveniently also be referred to as ‘base gasoline’.
  • Gasolines typically comprise mixtures of hydrocarbons boiling in the range from 25 to 230° C. (EN-ISO 3405), the optimal ranges and distillation curves typically varying according to climate and season of the year.
  • the hydrocarbons in a gasoline may be derived by any means known in the art, conveniently the hydrocarbons may be derived in any known manner from straight-run gasoline, synthetically-produced aromatic hydrocarbon mixtures, thermally or catalytically cracked hydrocarbons, hydro-cracked petroleum fractions, catalytically reformed hydrocarbons or mixtures of these.
  • the specific distillation curve, hydrocarbon composition, research octane number (RON) and motor octane number (MON) of the gasoline are not critical.
  • gasolines comprise components selected from one or more of the following groups; saturated hydrocarbons, olefinic hydrocarbons, aromatic hydrocarbons, and oxygenated hydrocarbons.
  • the gasoline may comprise a mixture of saturated hydrocarbons, olefinic hydrocarbons, aromatic hydrocarbons, and, optionally, oxygenated hydrocarbons.
  • the olefinic hydrocarbon content of the gasoline is in the range of from 0 to 40 percent by volume based on the gasoline (ASTM D1319); preferably, the olefinic hydrocarbon content of the gasoline is in the range of from 0 to 30 percent by volume based on the gasoline, more preferably, the olefinic hydrocarbon content of the gasoline is in the range of from 0 to 20 percent by volume based on the gasoline.
  • the aromatic hydrocarbon content of the gasoline is in the range of from 0 to 70 percent by volume based on the gasoline (ASTM D1319), for instance the aromatic hydrocarbon content of the gasoline is in the range of from 10 to 60 percent by volume based on the gasoline; preferably, the aromatic hydrocarbon content of the gasoline is in the range of from 0 to 50 percent by volume based on the gasoline, for instance the aromatic hydrocarbon content of the gasoline is in the range of from 10 to 50 percent by volume based on the gasoline.
  • the benzene content of the gasoline is at most 10 percent by volume, more preferably at most 5 percent by volume, especially at most 1 percent by volume based on the gasoline.
  • the gasoline preferably has a low or ultra low sulphur content, for instance at most 1000 ppmw (parts per million by weight), preferably no more than 500 ppmw, more preferably no more than 100, even more preferably no more than 50 and most preferably no more than even 10 ppmw.
  • the gasoline also preferably has a low total lead content, such as at most 0.005 g/l, most preferably being lead free—having no lead compounds added thereto (i.e. unleaded).
  • the oxygen content of the gasoline may be up to 35 percent by weight (EN 1601) (e.g. ethanol per se) based on the gasoline.
  • the oxygen content of the gasoline may be up to 25 percent by weight, preferably up to 10 percent by weight.
  • the oxygenate concentration will have a minimum concentration selected from any one of 0, 0.2, 0.4, 0.6, 0.8, 1.0, and 1.2 percent by weight, and a maximum concentration selected from any one of 5, 4.5, 4.0, 3.5, 3.0, and 2.7 percent by weight.
  • oxygenated hydrocarbons examples include alcohols, ethers, esters, ketones, aldehydes, carboxylic acids and their derivatives, and oxygen containing heterocyclic compounds.
  • the oxygenated hydrocarbons that may be incorporated into the gasoline are selected from alcohols (such as methanol, ethanol, propanol, iso-propanol, butanol, tert-butanol and iso-butanol), ethers (preferably ethers containing 5 or more carbon atoms per molecule, e.g., methyl tert-butyl ether) and esters (preferably esters containing 5 or more carbon atoms per molecule); a particularly preferred oxygenated hydrocarbon is ethanol.
  • oxygenated hydrocarbons When oxygenated hydrocarbons are present in the gasoline, the amount of oxygenated hydrocarbons in the gasoline may vary over a wide range.
  • gasolines comprising a major proportion of oxygenated hydrocarbons are currently commercially available in countries such as Brazil and U.S.A, e.g. ethanol per se and E85, as well as gasolines comprising a minor proportion of oxygenated hydrocarbons, e.g. E10 and E5. Therefore, the gasoline may contain up to 100 percent by volume oxygenated hydrocarbons.
  • the amount of oxygenated hydrocarbons present in the gasoline is selected from one of the following amounts: up to 85 percent by volume; up to 65 percent by volume; up to 30 percent by volume; up to 20 percent by volume; up to 15 percent by volume; and, up to 10 percent by volume, depending upon the desired final formulation of the gasoline.
  • the gasoline may contain at least 0.5, 1.0 or 2.0 percent by volume oxygenated hydrocarbons.
  • gasolines which have an olefinic hydrocarbon content of from 0 to 20 percent by volume (ASTM D1319), an oxygen content of from 0 to 5 percent by weight (EN 1601), an aromatic hydrocarbon content of from 0 to 50 percent by volume (ASTM D1319) and a benzene content of at most 1 percent by volume.
  • the base gasoline or the gasoline composition of the present invention may conveniently additionally include one or more fuel additive.
  • concentration and nature of the fuel additive(s) that may be included in the base gasoline or the gasoline composition of the present invention is not critical.
  • suitable types of fuel additives that can be included in the base gasoline or the gasoline composition of the present invention include anti-oxidants, corrosion inhibitors, detergents, dehazers, antiknock additives, metal deactivators, valve-seat recession protectant compounds, dyes, friction modifiers, carrier fluids, diluents and markers. Examples of suitable such additives are described generally in U.S. Pat. No. 5,855,629.
  • the fuel additives can be blended with one or more diluents or carrier fluids, to form an additive concentrate, the additive concentrate can then be admixed with the base gasoline or the gasoline composition of the present invention.
  • the (active matter) concentration of any additives present in the base gasoline or the gasoline composition of the present invention is preferably up to 1 percent by weight, more preferably in the range from 5 to 1000 ppmw, advantageously in the range of from 75 to 300 ppmw, such as from 95 to 150 ppmw.
  • the base fuel used is a diesel fuel
  • the diesel fuel used as the base fuel in the present invention includes diesel fuels for use in automotive compression ignition engines, as well as in other types of engine such as for example marine, railroad and stationary engines.
  • the diesel fuel used as the base fuel in the liquid fuel composition of the present invention may conveniently also be referred to as ‘diesel base fuel’.
  • the diesel base fuel may itself comprise a mixture of two or more different diesel fuel components, and/or be additivated as described below.
  • Such diesel fuels will contain one or more base fuels which may typically comprise liquid hydrocarbon middle distillate gas oil(s), for instance petroleum derived gas oils.
  • base fuels which may typically comprise liquid hydrocarbon middle distillate gas oil(s), for instance petroleum derived gas oils.
  • Such fuels will typically have boiling points within the usual diesel range of 150 to 400° C., depending on grade and use. They will typically have a density from 750 to 1000 kg/m 3 , preferably from 780 to 860 kg/m 3 , at 15° C. (e.g. ASTM D4502 or IP 365) and a cetane number (ASTM D613) of from 35 to 120, more preferably from 40 to 85. They will typically have an initial boiling point in the range 150 to 230° C. and a final boiling point in the range 290 to 400° C. Their kinematic viscosity at 40° C. (ASTM D445) might suitably be from 1.2 to 4.5 mm 2 /s.
  • An example of a petroleum derived gas oil is a Swedish Class 1 base fuel, which will have a density from 800 to 820 kg/m 3 at 15° C. (SS-EN ISO 3675, SS-EN ISO 12185), a T95 of 320° C. or less (SS-EN ISO 3405) and a kinematic viscosity at 40° C. (SS-EN ISO 3104) from 1.4 to 4.0 mm 2 /s, as defined by the Swedish national specification EC1.
  • non-mineral oil based fuels such as biofuels or Fischer-Tropsch derived fuels
  • Fischer-Tropsch fuels may for example be derived from natural gas, natural gas liquids, petroleum or shale oil, petroleum or shale oil processing residues, coal or biomass.
  • the amount of Fischer-Tropsch derived fuel used in the diesel fuel may be from 0% to 100% v of the overall diesel fuel, preferably from 5% to 100% v, more preferably from 5% to 75% v. It may be desirable for such a diesel fuel to contain 10% v or greater, more preferably 20% v or greater, still more preferably 30% v or greater, of the Fischer-Tropsch derived fuel. It is particularly preferred for such diesel fuels to contain 30 to 75% v, and particularly 30 or 70% v, of the Fischer-Tropsch derived fuel. The balance of the diesel fuel is made up of one or more other diesel fuel components.
  • Such a Fischer-Tropsch derived fuel component is any fraction of the middle distillate fuel range, which can be isolated from the (optionally hydrocracked) Fischer-Tropsch synthesis product. Typical fractions will boil in the naphtha, kerosene or gas oil range. Preferably, a Fischer-Tropsch product boiling in the kerosene or gas oil range is used because these products are easier to handle in for example domestic environments. Such products will suitably comprise a fraction larger than 90 wt % which boils between 160 and 400° C., preferably to about 370° C.
  • Fischer-Tropsch derived kerosene and gas oils are described in EP-A-0583836, WO-A-97/14768, WO-A-97/14769, WO-A-00/11116, WO-A-00/11117, WO-A-01/83406, WO-A-01/83648, WO-A-01/83647, WO-A-01/83641, WO-A-00/20535, WO-A-00/20534, EP-A-1101813, U.S. Pat. No. 5,766,274, U.S. Pat. No. 5,378,348, U.S. Pat. No. 5,888,376 and U.S. Pat. No. 6,204,426 which disclosures are herein incorporated by reference.
  • the Fischer-Tropsch product will suitably contain more than about 80 wt % and more suitably more than about 95 wt % iso and normal paraffins and less than about 1 wt % aromatics, the balance being naphthenics compounds.
  • the content of sulphur and nitrogen will be very low and normally below the detection limits for such compounds. For this reason the sulphur content of a diesel fuel composition containing a Fischer-Tropsch product may be very low.
  • the diesel fuel composition preferably contains no more than 5000 ppmw sulphur, more preferably no more than 500 ppmw, or no more than 350 ppmw, or no more than 150 ppmw, or no more than 100 ppmw, or no more than 70 ppmw, or no more than 50 ppmw, or no more than 30 ppmw, or no more than 20 ppmw, or most preferably no more than 15 ppmw sulphur.
  • the diesel base fuel may itself be additivated (additive-containing) or unadditivated (additive-free). If additivated, e.g. at the refinery, it will contain minor amounts of one or more additives selected for example from anti-static agents, pipeline drag reducers, flow improvers (e.g. ethylene/vinyl acetate copolymers or acrylate/maleic anhydride copolymers), lubricity additives, antioxidants and wax anti-settling agents.
  • additives selected for example from anti-static agents, pipeline drag reducers, flow improvers (e.g. ethylene/vinyl acetate copolymers or acrylate/maleic anhydride copolymers), lubricity additives, antioxidants and wax anti-settling agents.
  • Detergent-containing diesel fuel additives are known and commercially available. Such additives may be added to diesel fuels at levels intended to reduce, remove, or slow the build up of engine deposits.
  • detergents suitable for use in diesel fuel additives for the present purpose include polyolefin substituted succinimides or succinamides of polyamines, for instance polyisobutylene succinimides or polyisobutylene amine succinamides, aliphatic amines, Mannich bases or amines and polyolefin (e.g. polyisobutylene) maleic anhydrides.
  • Succinimide dispersant additives are described for example in GB-A-960493, EP-A-0147240, EP-A-0482253, EP-A-0613938, EP-A-0557516 and WO-A-98/42808.
  • Particularly preferred are polyolefin substituted succinimides such as polyisobutylene succinimides.
  • the diesel fuel additive mixture may contain other components in addition to the detergent.
  • lubricity enhancers e.g. alkoxylated phenol formaldehyde polymers
  • anti-foaming agents e.g. polyether-modified polysiloxanes
  • ignition improvers cetane improvers
  • cetane improvers e.g. 2-ethylhexyl nitrate (EHN), cyclohexyl nitrate, di-tert-butyl peroxide and those disclosed in U.S. Pat. No. 4,208,190 at column 2, line 27 to column 3, line 21
  • anti-rust agents e.g.
  • a propane-1,2-diol semi-ester of tetrapropenyl succinic acid, or polyhydric alcohol esters of a succinic acid derivative the succinic acid derivative having on at least one of its alpha-carbon atoms an unsubstituted or substituted aliphatic hydrocarbon group containing from 20 to 500 carbon atoms, e.g. the pentaerythritol diester of polyisobutylene-substituted succinic acid); corrosion inhibitors; reodorants; anti-wear additives; anti-oxidants (e.g.
  • phenolics such as 2,6-di-tert-butylphenol, or phenylenediamines such as N,N′-di-sec-butyl-p-phenylenediamine); metal deactivators; combustion improvers; static dissipator additives; cold flow improvers; and wax anti-settling agents.
  • the diesel fuel additive mixture may contain a lubricity enhancer, especially when the diesel fuel composition has a low (e.g. 500 ppmw or less) sulphur content.
  • the lubricity enhancer is conveniently present at a concentration of less than 1000 ppmw, preferably between 50 and 1000 ppmw, more preferably between 70 and 1000 ppmw.
  • Suitable commercially available lubricity enhancers include ester- and acid-based additives.
  • Other lubricity enhancers are described in the patent literature, in particular in connection with their use in low sulphur content diesel fuels, for example in:
  • the diesel fuel composition may also be preferred for the diesel fuel composition to contain an anti-foaming agent, more preferably in combination with an anti-rust agent and/or a corrosion inhibitor and/or a lubricity enhancing additive.
  • the (active matter) concentration of each such additive component in the additivated diesel fuel composition is preferably up to 10000 ppmw, more preferably in the range from 0.1 to 1000 ppmw, advantageously from 0.1 to 300 ppmw, such as from 0.1 to 150 ppmw.
  • the (active matter) concentration of any dehazer in the diesel fuel composition will preferably be in the range from 0.1 to 20 ppmw, more preferably from 1 to 15 ppmw, still more preferably from 1 to 10 ppmw, advantageously from 1 to 5 ppmw.
  • the (active matter) concentration of any ignition improver present will preferably be 2600 ppmw or less, more preferably 2000 ppmw or less, conveniently from 300 to 1500 ppmw.
  • the (active matter) concentration of any detergent in the diesel fuel composition will preferably be in the range from 5 to 1500 ppmw, more preferably from 10 to 750 ppmw, most preferably from 20 to 500 ppmw.
  • the fuel additive mixture will typically contain a detergent, optionally together with other components as described above, and a diesel fuel-compatible diluent, which may be a mineral oil, a solvent such as those sold by Shell companies under the trade mark “SHELLSOL”, a polar solvent such as an ester and, in particular, an alcohol, e.g. hexanol, 2-ethylhexanol, decanol, isotridecanol and alcohol mixtures such as those sold by Shell companies under the trade mark “LINEVOL”, especially LINEVOL 79 alcohol which is a mixture of C 7-9 primary alcohols, or a C 12-14 alcohol mixture which is commercially available.
  • a diesel fuel-compatible diluent which may be a mineral oil, a solvent such as those sold by Shell companies under the trade mark “SHELLSOL”, a polar solvent such as an ester and, in particular, an alcohol, e.g. hexanol, 2-ethylhexanol, decan
  • the total content of the additives in the diesel fuel composition may be suitably between 0 and 10000 ppmw and preferably below 5000 ppmw.
  • amounts (concentrations, % vol, ppmw, % wt) of components are of active matter, i.e. exclusive of volatile solvents/diluent materials.
  • the liquid fuel composition of the present invention is produced by admixing the one or more poly(hydroxycarboxylic acid) amide salt derivatives with a base fuel suitable for use in an internal combustion engine. If the base fuel to which the one or more poly(hydroxycarboxylic acid) amide salt derivatives is admixed is a gasoline, then the liquid fuel composition produced is a gasoline composition; likewise, if the base fuel to which the one or more poly(hydroxycarboxylic acid) amide salt derivatives is admixed is a diesel fuel, then the liquid fuel composition produced is a diesel fuel composition.
  • the amount of the one or more poly(hydroxycarboxylic acid) amide salt derivatives present in the liquid fuel composition of the present invention is at least 1 ppmw (part per million by weight), based on the overall weight of the liquid fuel composition. More preferably, the amount of the one or more poly(hydroxycarboxylic acid) amide salt derivatives present in the liquid fuel composition of the present invention additionally accords with one or more of the parameters (i) to (xx) listed below:
  • the amount of the one or more poly(hydroxycarboxylic acid) amide salt derivatives present in the liquid fuel composition of the present invention may also be at least 200 ppmw, at least 300 ppmw, at least 400 ppmw, at least 500 ppmw, or even at least 1000 ppmw.
  • the use of the one or more poly(hydroxycarboxylic acid) amide salt derivatives in the liquid fuel compositions can provide significant benefits in terms of improved lubricity of the liquid fuel composition, in particular when the liquid fuel composition is gasoline, relative to the liquid base fuel.
  • improve/improving lubricity used herein, it is meant that the wear scar produced using a high frequency reciprocating rig (HFRR) is reduced.
  • HFRR high frequency reciprocating rig
  • the use of the one or more poly(hydroxycarboxylic acid) amide salt derivatives in liquid fuel compositions can also provide benefits in terms of engine cleanliness, in particular in terms of improved inlet valve deposit keep clean and/or injector nozzle keep clean performance, of an internal combustion engine being fuelled by the liquid fuel composition of the present invention relative to the internal combustion engine being fuelled by the liquid base fuel.
  • improved/improving inlet valve deposit keep clean performance it is meant that the weight of deposit formed on the inlet valve of the engine is reduced relative to the base fuel not containing the one or more poly(hydroxycarboxylic acid) amide salt derivatives.
  • improve/improving injector nozzle keep clean performance it is meant that the amount of deposit formed on the injector nozzle of the engine is reduced as measured by the loss of engine torque.
  • liquid fuel compositions can also provide benefits in terms improved fuel economy of an internal combustion engine being fuelled by the liquid fuel composition of the present invention relative to the internal combustion engine being fuelled by the liquid base fuel.
  • the present invention therefore also provides a method of improving the lubricity of a liquid base fuel suitable for use in an internal combustion engine, comprising admixing one or more poly(hydroxycarboxylic acid) amide salt derivatives with a major portion of the liquid base fuel suitable for use in an internal combustion engine; a method of improving the inlet valve deposit clean up performance of a liquid base fuel suitable for use in an internal combustion engine, comprising admixing one or more poly(hydroxycarboxylic acid) amide salt derivatives with a major portion of the liquid base fuel suitable for use in an internal combustion engine; a method of improving the injector nozzle keep clean performance of a liquid base fuel suitable for use in an internal combustion engine, comprising admixing one or more poly(hydroxycarboxylic acid) amide salt derivatives with a major portion of the liquid base fuel suitable for use in an internal combustion engine; and, a method of improving the fuel economy performance of a liquid base fuel suitable for use in an internal combustion engine, comprising admixing one or more poly(hydroxycarboxy
  • liquid fuel compositions can also provide benefits in terms improving the lubricant performance of an internal combustion engine being fuelled by the liquid fuel composition of the present invention relative to the internal combustion engine being fuelled by the liquid base fuel.
  • the improvement in the lubricant performance of the internal combustion engine fuelled by a liquid fuel composition according to the present invention can be observed by the a reduction in the levels of sludge and varnish on specific engine parts, such as sludge on rocker arm covers, cam baffles, timing chain covers, oil pans, oil pan baffles, and valve decks, and varnish on piston skirts and cam baffles.
  • specific engine parts such as sludge on rocker arm covers, cam baffles, timing chain covers, oil pans, oil pan baffles, and valve decks, and varnish on piston skirts and cam baffles.
  • the use of the one or more poly(hydroxycarboxylic acid) amide salt derivatives in a gasoline compositions can provide benefits in terms inhibiting specific sludge and varnish deposit formation, as measured by ASTM D 6593-07, of an internal combustion engine being fuelled by the gasoline composition of the present invention relative to the internal combustion engine being fuelled by the gasoline base fuel.
  • the present invention also provides a method of improving the performance of the lubricant of an internal combustion engine, said method comprising fuelling an internal combustion engine containing the engine lubricant with a liquid fuel composition according to the present invention.
  • the use of one or more poly(hydroxycarboxylic acid) amide salt derivatives wherein the anion is a non-sulfur-containing anion in a liquid fuel composition can have the additional advantage of improved phosphorus volatility properties of the engine lubricant of an internal combustion engine fuelled by the liquid fuel composition compared to the phosphorus volatility properties of the engine lubricant when one or more poly(hydroxycarboxylic acid) amide salt derivatives wherein the anion is a sulfur-containing anion is used in the liquid fuel composition.
  • the phosphorus volatility properties of the engine lubricant can conveniently be measured according to the phosphorus emission index (PEI) test, which is also known as the “Selby-Noack PEI test”. This test has been described in T. W. Selby, R. J. Bosch and D.C. Fee, “Continued Studies of the Causes of Engine Oil, Phosphorus Volatility—Part 2”. SAE 2007-01-1073, the teaching of which is hereby incorporated by specific reference.
  • the “Selby-Noack PEI test” is similar to the “Noack procedure” as described in ASTM D 5800, procedure C, but deviates in duration (16 hours instead of 24 hours for the Noack procedure) and temperature (250° C. for the Noack procedure).
  • the PEI is an approximation of the quantity of phosphorus (mg) obtained from 1 kg of fluid, it has no unit.
  • improved phosphorus volatility properties it is meant that the PEI is lower than the PEI result it is being compared to.
  • the present invention also provides the use of one or more poly(hydroxycarboxylic acid) amide salt derivatives wherein the anion is a non-sulfur-containing anion in a liquid fuel composition according to the present invention for improving the phosphorus volatility properties of an engine lubricant of an internal combustion engine fuelled by the liquid fuel composition compared to the phosphorus volatility properties of the engine lubricant when one or more poly(hydroxycarboxylic acid) amide salt derivatives wherein the anion is a sulfur-containing anion is used in the liquid fuel composition.
  • the present invention further provides a method of operating an internal combustion engine, which method involves introducing into a combustion chamber of the engine a liquid fuel composition according to the present invention.
  • the one or more poly(hydroxycarboxylic acid) amide salt derivatives of the present invention may also be conveniently incorporated into lubricant formulations, especially engine crank case lubricant formulations.
  • hyperdispersants were poly(hydroxycarboxylic acid) amide salt derivatives, wherein the anion is a methyl sulphate anion, according to the present invention were products available commercially from Shanghai Sanzheng Polymer Company under the trade designations “CH-5” and “CH-7”. Certain measured properties of both CH-5 and CH-7 are given in Table 1 below:
  • CH-5 and CH-7 hyperdispersants described above were blended into a base fuel selected from the gasoline, diesel, GTL diesel and Swedish Class I diesel base fuels described in Tables 2 and 3 below, in various amounts.
  • the lubricity of the diesel fuel compositions was determined using the HFRR test used described in ISO 12156-1.
  • the lubricity of the gasoline compositions was determined by using a modified HFRR test.
  • the modified HFRR test is based on ISO 12156-1 using a PCS Instruments HFRR supplemented with the PCS Instruments Gasoline Conversion Kit, and using a fluid volume of 15.0 ml (+/ ⁇ 0.2 ml), a fluid temperature of 25.0° C. (+/ ⁇ 1° C.), and wherein a PTFE cover is used to cover the test sample in order to minimise evaporation.
  • Inlet valve deposit keep clean tests were performed for two gasoline compositions prepared by blending a base gasoline as described in Table 5 below with 400 ppmw and 1000 ppmw of the CH-5 hyperdispersant.
  • the IVD test was performed in a Toyota 2.0 L 3S-FE bench engine using the CEC-F-05-A-93 M102E operating cycle modified by BMEP to the torque conditions detailed in Table 6 below.
  • the Toyota engine has been modified to concurrently run two fuel systems, one fuelling cylinders 1 and 2 and a second fuelling cylinders 3 and 4.
  • the engine starts with clean valves and combustion chamber and is run for 69 hr on the test fuels. At the end of the 69 hours the engine is stripped, the valves weighed to determine the level of deposits.
  • the gasoline containing 400 and 1000 ppmw respectively of CH-5 was tested in the Toyota 3S-FE dual fuelled engine with the 400 ppmw CH-5 gasoline test blend in cylinders 1 and 2 and the 1000 ppmw CH-5 gasoline test blend in cylinders 3 and 4.
  • the average weight of the inlet valve deposits for cylinders 1 and 2 was 194.6 mg and for cylinders 3 and 4 was 130.0 mg.
  • An average level of deposit observed with a gasoline containing no additives in a 69 hour test is typically about 200 mg.
  • the injector nozzle keep clean performance of the CH-5 hyperdispersant in diesel fuel was assessed using the CEC SG-F-098 test procedure.
  • the diesel fuel used in the test procedure contained 300 ppmw of the CH-5 hyperdispersant. In the test, up until 24 hours no power loss was observed and at 32 hours a power loss equating to 3% was observed. At this point the equivalent power loss for the reference fuel was 9%.
  • the funnel was shaken and allowed to stand until there was clear separation between the two layers.
  • the organic bottom layer was collected and added to 250 ml of fresh 1M KOH in a separation funnel. Again, the organic bottom layer was collected, dried over MgSO 4 and concentrated in vacuo. About 6 gram of poly(hydroxycarboxylic acid) amide salt derivative wherein the anion X q ⁇ is OH was obtained.
  • the obtained poly(hydroxycarboxylic acid) amide salt derivative had a TBN content of 7.4 mg ⁇ KOH/g (according to ASTM D 4739).
  • the “CH-5” product (see Example E) was ion-exchanged with a sodium salicylate (available from Sigma-Aldrich Chemical Company, Gillingham, United Kingdom) in a ion-exchange column, whilst using 1:3 MeOH:CHCl 3 as an eluent.
  • a sodium salicylate available from Sigma-Aldrich Chemical Company, Gillingham, United Kingdom
  • a column was prepared using 500 gram Dowex 1 ⁇ 8 ion-exchange resin (200-400 mesh, strongly basic Cl ⁇ form; CAS nr [69011-19-4]) which was washed in 1 l of deionised water.
  • the washed Dowex resin was then loaded as a suspension onto a column using 1 l of 1:1 MeOH:de-ionised water.
  • the resin was then washed with 4 bed volumes of 1:1 methanol/de-ionised water and loaded with a 30 wt. % solution of the sodium salicylate salt of in a small amount of MeOH.
  • the obtained poly(hydroxycarboxylic acid) amide salt derivative had a TBN content of 8.2 mg ⁇ KOH/g (according to ASTM D 4739).
  • Example F Similar to Example F, a poly(hydroxycarboxylic acid) amide salt derivative was obtained wherein the anion X q ⁇ is a phenate. To this end sodium phenoate (available from Sigma-Aldrich Chemical Company, Gillingham, United Kingdom) was used.
  • the obtained poly(hydroxycarboxylic acid) amide salt derivative had a TBN content of 8.5 mg ⁇ KOH/g (according to ASTM D 4739).
  • Example F Similar to Example F, a poly(hydroxycarboxylic acid) amide salt derivative was obtained wherein the anion X q ⁇ is an oleate. To this end sodium oleate (available from Sigma-Aldrich Chemical Company, Gillingham, United Kingdom) was used.
  • the obtained poly(hydroxycarboxylic acid) amide salt derivative had a TBN content of 7.9 mg ⁇ KOH/g (according to ASTM D 4739).
  • Example F Similar to Example F, a poly(hydroxycarboxylic acid) amide salt derivative was obtained wherein the anion X q ⁇ is an acetate. To this end sodium acetate (available from Sigma-Aldrich Chemical Company, Gillingham, United Kingdom) was used.
  • the obtained poly(hydroxycarboxylic acid) amide salt derivative had a TBN content of 8.5 mg ⁇ KOH/g (according to ASTM D 4739).
  • crankcase lubricant of an engine fuelled using a liquid fuel composition according to the present invention was assessed using the Sequence VG test, ASTM D 6593-07.
  • the base fuel used for both poly(hydroxycarboxylic acid) amide salt derivatives was an ASTM VG base fuel.
  • Fuel “Base” is ASTM VG base fuel.
  • Fuel “F-A” is “Base”+500 ppmw of “CH-5”.
  • Fuel “F-B” is “Base”+200 ppmw of Example F.
  • Lubricant “L-A” is an SF grade lubricant.
  • Lubricant “L-B” is a SL/CF grade lubricant.
  • the results of the Sequence VG tests are provided in Table 7 below.
  • the “merit” rating used in the results is on a scale of 0 to 10, with 10 representing the rating of the condition of the component when new, and a single number increase in the “merit” rating represents a reduction in the sludge or varnish by half.

Abstract

The present invention provides a liquid fuel composition comprising:
    • a) a liquid base fuel suitable for use in an internal combustion engine; and
    • b) one or more poly(hydroxycarboxylic acid) amide salt derivatives having formula (III):

[Y—CO[O-A-CO]n-Zr-R+]mpXq−  (III)
    • wherein Y is hydrogen or an optionally substituted hydrocarbyl group, A is a divalent optionally substituted hydrocarbyl group, n is from 1 to 100, m is from 1 to 4, q is from 1 to 4 and p is an integer such that pq=m, Z is an optionally substituted divalent bridging group which is attached to the carbonyl group through a nitrogen atom, r is 0 or 1, R+ is an ammonium group and Xq− is an anion.

Description

    FIELD OF THE INVENTION
  • The present invention relates to liquid fuel compositions comprising a major portion of a base fuel suitable for use in an internal combustion engine, in particular liquid fuel compositions comprising a major portion of a base fuel suitable for use in an internal combustion engine and a hyperdispersant.
  • BACKGROUND OF THE INVENTION
  • EP 0164817 A2 discloses a surfactant comprising a carboxylic acid ester or amide carrying a terminal strong acid group selected from carboxymethyl, sulphate, sulphonate, phosphate and phosphonate, suitable for stabilising dispersions of solids in organic liquids and oil/water emulsions. A preferred species of the surfactant is a poly(hydroxyalkanecarboxylic acid) having the strong acid group attached, either directly or through a linking group, to a terminal hydroxy or carboxylic acid group. The use of such surfactants in fuels is not disclosed therein.
  • EP 0233684 A1 discloses an ester or polyester having (i) a terminal group containing at least two aliphatic carbon-carbon double bonds and (ii) an acidic or basic amino group which is suitable for use as a dispersant for solids in organic liquids. The use of such surfactants in fuels is not disclosed therein.
  • GB 2197312 A discloses oil soluble dispersant additives, wherein said dispersant additives are poly (C5-C9 lactone) adducts which have been prepared by first reacting a C5-C9 lactone with a polyamine, a polyol or an amino alcohol to form an intermediate adduct, whereafter the intermediate adduct is reacted with an aliphatic hydrocarbyl monocarboxylic or dicarboxylic acylating agent having from about 1 to about 165 total carbon atoms. The use of the dispersant additives in lubricating oils and fuels is also disclosed in GB 2197312 A.
  • EP 0802255 A2 discloses hydroxyl group containing acylated nitrogen compounds which are useful as low chlorine containing additives for lubricating oils and normally liquid fuels and a process for preparing the compounds.
  • WO 00/34418 A1 discloses the use of poly(hydroxycarboxylic acid)amide or -ester derivatives in fuel compositions as a lubricity additive. It is also disclosed in WO 00/34418 A1 that the use of the poly(hydroxycarboxylic acid)amide or -ester derivatives disclosed therein may also result in attaining one or more of a number of effects such as inlet system cleanliness (intake valves, fuel injectors, carburetors), combustion chamber cleanliness (in each case either or both of keep clean and clean-up effects), anti-corrosion (including anti-rust) and reduction or elimination of valve-stick.
  • SUMMARY OF THE INVENTION
  • The present invention provides a liquid fuel composition comprising:
      • a) a liquid base fuel suitable for use in an internal combustion engine; and
      • b) one or more poly(hydroxycarboxylic acid) amide salt derivatives having formula (III):

  • [Y—CO[O-A-CO]n-Zr-R+]mpXq−  (III)
  • wherein Y is hydrogen or an optionally substituted hydrocarbyl group, A is a divalent optionally substituted hydrocarbyl group, n is from 1 to 100, m is from 1 to 4, q is from 1 to 4 and p is an integer such that pq=m, Z is an optionally substituted divalent bridging group which is attached to the carbonyl group through a nitrogen atom, r is 0 or 1, R+ is an ammonium group and Xq− is an anion.
  • The present invention further provides a method for preparing a liquid fuel composition of the present invention comprising admixing the one or more poly(hydroxycarboxylic acid) amide salt derivatives with a base fuel suitable for use in an internal combustion engine.
  • The present invention yet further provides a method of operating an internal combustion engine, which method involves introducing into a combustion chamber of the engine a liquid fuel composition according to the present invention
  • It has now been found that the use of poly(hydroxycarboxylic acid) amide salt derivatives can also surprisingly provides benefits in terms of improving the lubricity of liquid fuel compositions incorporated them.
  • DETAILED DESCRIPTION OF THE INVENTION
  • The liquid fuel composition of the present invention comprises a base fuel suitable for use in an internal combustion engine and one or more poly(hydroxycarboxylic acid) amide salt derivatives. Typically, the base fuel suitable for use in an internal combustion engine is a gasoline or a diesel fuel, and therefore the liquid fuel composition of the present invention is typically a gasoline composition or a diesel fuel composition.
  • The poly(hydroxycarboxylic acid) amide salt derivatives used in the present invention may also be referred to as hyperdispersants.
  • The one or more poly(hydroxycarboxylic acid) amide salt derivatives in the liquid fuel compositions of the present invention are poly(hydroxycarboxylic acid) amide salt derivatives having formula (III):

  • [Y—CO[O-A-CO]n-Zr-R+]mpXq−  (III)
  • wherein Y is hydrogen or optionally substituted hydrocarbyl group, A is a divalent optionally substituted hydrocarbyl group, n is from 1 to 100, m is from 1 to 4, q is from 1 to 4 and p is an integer such that pq=m, Z is an optionally substituted divalent bridging group which is attached to the carbonyl group through a nitrogen atom, r is 0 or 1, R+ is an ammonium group and Xq− is an anion.
  • R+ may be a primary, secondary, tertiary or quaternary ammonium group. R+ is preferably a quaternary ammonium group.
  • In formula (III), A is preferably a divalent straight chain or branched hydrocarbyl group as hereafter described for formulae (I) and (II) below.
  • That is to say, in formula (III), A is preferably an optionally substituted aromatic, aliphatic or cycloaliphatic straight chain or branched divalent hydrocarbyl group. More preferably, A is an arylene, alkylene or alkenylene group, in particular an arylene, alkylene or alkenylene group containing in the range of from 4 to 25 carbon atoms, more preferably in the range of from 6 to 25 carbon atoms, more preferably in the range of from 8 to 24 carbon atoms, more preferably in the range of from 10 to 22 carbon atoms, and most preferably in the range of from 12 to 20 carbon atoms.
  • Preferably, in said compound of formula (III), there are at least 4 carbon atoms, more preferably at least 6 carbon atoms, and even more preferably in the range of from 8 to 14 carbon atoms connected directly between the carbonyl group and the oxygen atom derived from the hydroxyl group.
  • In the compound of formula (III), the optional substituents in the group A are preferably selected from hydroxy, halo or alkoxy groups, especially C1-4 alkoxy groups.
  • In formula (III) (and formula (I)), n is in the range of from 1 to 100. Preferably, the lower limit of the range for n is 1, more preferably 2, even more preferably 3; preferably the upper limit of the range for n is 100, more preferably 60, more preferably 40, more preferably 20, and even more preferably 10 (i.e. n may be selected from any of the following ranges: from 1 to 100; from 2 to 100; from 3 to 100; from 1 to 60; from 2 to 60; from 3 to 60; from 1 to 40; from 2 to 40; from 3 to 40; from 1 to 20; from 2 to 20; from 3 to 20; from 1 to 10; from 2 to 10; and, from 3 to 10).
  • In formula (III), Y is preferably an optionally substituted hydrocarbyl group as hereinafter described for formula (I).
  • That is to say, the optionally substituted hydrocarbyl group Y in formula (III) is preferably aryl, alkyl or alkenyl containing up to 50 carbon atoms, more preferably in the range of from 7 to 25 carbon atoms. For example, the optionally substituted hydrocarbyl group Y may be conveniently selected from heptyl, octyl, undecyl, lauryl, heptadecyl, heptadenyl, heptadecadienyl, stearyl, oleyl and linoleyl.
  • Other examples of said optionally substituted hydrocarbyl group Y in formula (III) herein include C4-8 cycloalkyls such as cyclohexyl; polycycloalkyls such as polycyclic terpenyl groups which are derived from naturally occurring acids such as abietic acid; aryls such as phenyl; aralkyls such as benzyl; and polyaryls such as naphthyl, biphenyl, stibenzyl and phenylmethylphenyl.
  • In the present invention, the optionally substituted hydrocarbyl group Y in formula (III) may contain one or more functional groups such as carbonyl, carboxyl, nitro, hydroxy, halo, alkoxy, amino, preferably tertiary amino (no N—H linkages), oxy, cyano, sulphonyl and sulphoxyl. The majority of the atoms, other than hydrogen, in substituted hydrocarbyl groups are generally carbon, with the heteroatoms (e.g., oxygen, nitrogen and sulphur) generally representing only a minority, about 33% or less, of the total non-hydrogen atoms present.
  • Those skilled in the art will appreciate that functional groups such as hydroxy, halo, alkoxy, nitro and cyano in a substituted hydrocarbyl group Y will displace one of the hydrogen atoms of the hydrocarbyl, whilst functional groups such as carbonyl, carboxyl, tertiary amino (—N—), oxy, sulphonyl and sulphoxyl in a substituted hydrocarbyl group will displace a —CH— or —CH2— moiety of the hydrocarbyl.
  • More preferably, the hydrocarbyl group Y in formula (III) is unsubstituted or substituted by a group selected from hydroxy, halo or alkoxy group, even more preferably C1-4 alkoxy.
  • Most preferably, the optionally substituted hydrocarbyl group Y in formula (III) is a stearyl group, 12-hydroxystearyl group, an oleyl group or a 12-hydroxyoleyl group, and that derived from naturally occurring oil such as tall oil fatty acid.
  • In formula (III), Z is preferably an optionally substituted divalent bridging group represented by formula (IV)
  • Figure US20100024286A1-20100204-C00001
  • wherein R1 is hydrogen or a hydrocarbyl group and B is an optionally substituted alkylene group.
  • Examples of hydrocarbyl groups that may represent R1 include methyl, ethyl, n-propyl, n-butyl and octadecyl.
  • Examples of optionally substituted alkylene groups that may represent B include ethylene, trimethylene, tetramethylene and hexamethylene.
  • Examples of preferred Z moieties in formula (III) include —NHCH2CH2—, —NHCH2C(CH3)2CH2— and —NH(CH2)3—.
  • In formula (III), r is preferably 1, i.e. the poly(hydroxycarboxylic acid) amide salt derivative having formula (III) must contain the optionally substituted divalent bridging group Z.
  • Preferably, R+ may be represented by formula (V)
  • Figure US20100024286A1-20100204-C00002
  • wherein R2, R3 and R4 may be selected from hydrogen and alkyl groups such as methyl.
  • The anion Xq− of the compound of formula (III) is not critical and can be any anion (or mixture of anions) suitable to balance the positive charge of the poly(hydroxycarboxylic acid) amide cation.
  • The anion Xq− of the compound of formula (III) may conveniently be a sulphur-containing anion, such as an anion selected from sulphate and sulphonate anions.
  • However, since it is desirable to maintain a low sulphur content in gasoline and diesel fuels, the use of non-sulphur-containing anions in the compounds of formula (III) may be desirable depending upon the concentration of sulphur in the liquid base fuel and/or the desired concentration of sulphur in the liquid fuel composition containing the one or more poly(hydroxycarboxylic acid) amide salt derivatives.
  • Therefore, the anion Xq− of the compound of formula (III) can also be any non-sulphur-containing anion (or mixture of anions) suitable to balance the positive charge of the poly(hydroxycarboxylic acid) amide cation, such as a non-sulphur-containing organic anion or a non-sulphur-containing inorganic anion.
  • Non-limiting examples of suitable anions are OH, CH, NH3 , HCO3 , HCOO, CH3COO, H, BO3 3−, cO3 2−, C2H3O2 , HCO2−, C2O4 2−, HC2O4 , NO2 , NO2 , N3−, NH2 , O2−, O2 2−, BeF3 , F, Na, [Al(H2O)2(OH)4], SiO3 , SiF6 , H2PO4 , P3−, PO4 3−, HPO4 2−, Cl, ClO3 , ClO4 , ClO, KO, SbOH6 , SnCl6 2−, [SnTe4]4−, CrO4 2−, Cr2O7 2−, MnO4 , NiCl6 2−, [Cu(CO3)2(OH)2]4−, AsO4 3−, Br, BrO3 , IO3 , I, CN, OCN, etc.
  • Suitable anions may also include anions derived from compounds containing a carboxylic acid group (e.g. a carboxylate anion), anions derived from compounds containing a hydroxyl group (e.g. an alkoxide, phenoxide or enolate anion), nitrogen based anions such as nitrate and nitrite, phosphorus based anions such as phosphates and phosphonates, or mixtures thereof.
  • Non-limiting examples of suitable anions derived from compounds containing a carboxylic acid group include acetate, oleate, salicylate anions, and mixtures thereof.
  • Non-limiting examples of suitable anions derived from compounds containing a hydroxyl group include phenate anions, and mixtures thereof.
  • In a preferred embodiment of the present invention, the anion Xq− is a non-sulfur-containing anion selected from the group consisting of OH, a phenate group, a salicylate group, an oleate group and an acetate group; more preferably the anion Xq− is OH.
  • The one or more poly(hydroxycarboxylic acid) amide salt derivatives may be obtained by reaction of an amine and a poly(hydroxycarboxylic acid) of formula (I)

  • Y—CO[O-A-CO]n—OH  (I)
  • wherein Y is hydrogen or optionally substituted hydrocarbyl group, A is a divalent optionally substituted hydrocarbyl group and n is from 1 to 100, with an acid or a quaternizing agent.
  • As used herein, the term “hydrocarbyl” represents a radical formed by removal of one or more hydrogen atoms from a carbon atom of a hydrocarbon (not necessarily the same carbon atoms in case more hydrogen atoms are removed).
  • Hydrocarbyl groups may be aromatic, aliphatic, acyclic or cyclic groups. Preferably, hydrocarbyl groups are aryl, cycloalkyl, alkyl or alkenyl, in which case they may be straight-chain or branched-chain groups.
  • Representative hydrocarbyl groups include phenyl, naphthyl, methyl, ethyl, butyl, pentyl, methylpentyl, hexenyl, dimethylhexyl, octenyl, cyclooctenyl, methylcyclooctenyl, dimethylcyclooctyl, ethylhexyl, octyl, isooctyl, dodecyl, hexadecenyl, eicosyl, hexacosyl, triacontyl and phenylethyl.
  • In the present invention, the phrase “optionally substituted hydrocarbyl” is used to describe hydrocarbyl groups optionally containing one or more “inert” heteroatom-containing functional groups. By “inert” is meant that the functional groups do not interfere to any substantial degree with the function of the compound.
  • The optionally substituted hydrocarbyl group Y in formula (I) herein is preferably aryl, alkyl or alkenyl containing up to 50 carbon atoms, more preferably in the range of from 7 to 25 carbon atoms. For example, the optionally substituted hydrocarbyl group Y may be conveniently selected from heptyl, octyl, undecyl, lauryl, heptadecyl, heptadenyl, heptadecadienyl, stearyl, oleyl and linoleyl.
  • Other examples of said optionally substituted hydrocarbyl group Y in formula (I) herein include C4-8 cycloalkyls such as cyclohexyl; polycycloalkyls such as polycyclic terpenyl groups which are derived from naturally occurring acids such as abietic acid; aryls such as phenyl; aralkyls such as benzyl; and polyaryls such as naphthyl, biphenyl, stibenzyl and phenylmethylphenyl.
  • In the present invention, the optionally substituted hydrocarbyl group Y may contain one or more functional groups such as carbonyl, carboxyl, nitro, hydroxy, halo, alkoxy, tertiary amino (no N—H linkages), oxy, cyano, sulphonyl and sulphoxyl. The majority of the atoms, other than hydrogen, in substituted hydrocarbyl groups are generally carbon, with the heteroatoms (e.g., oxygen, nitrogen and sulphur) generally representing only a minority, about 33% or less, of the total non-hydrogen atoms present.
  • Those skilled in the art will appreciate that functional groups such as hydroxy, halo, alkoxy, nitro and cyano in a substituted hydrocarbyl group Y will displace one of the hydrogen atoms of the hydrocarbyl, whilst functional groups such as carbonyl, carboxyl, tertiary amino (—N—), oxy, sulphonyl and sulphoxyl in a substituted hydrocarbyl group will displace a —CH— or —CH2— moiety of the hydrocarbyl.
  • The hydrocarbyl group Y in formula (I) is more preferably unsubstituted or substituted by a group selected from hydroxy, halo or alkoxy group, even more preferably C1-4 alkoxy.
  • Most preferably, the optionally substituted hydrocarbyl group Y in formula (I) is a stearyl group, 12-hydroxystearyl group, an oleyl group, a 12-hydroxyoleyl group or a group derived from naturally occurring oil such as tall oil fatty acid.
  • In one embodiment of the present invention, at least one of, or all of, the one or more poly(hydroxycarboxylic acid) amide salt derivatives are sulphur-containing poly(hydroxycarboxylic acid) amide salt derivatives.
  • In such an embodiment, said one or more poly(hydroxycarboxylic acid) amide salt derivatives preferably have a sulphur content of at most 2.5 wt. %, such as a sulphur content in the range of from 0.1 to 2.0 wt. %, conveniently in the range of from 0.6 to 1.2 wt. % sulphur, as measured by ICP-AES, based on the total weight of said poly(hydroxycarboxylic acid) amide salt derivatives.
  • In another embodiment of the present invention, the one or more poly(hydroxycarboxylic acid) amide salt derivatives are non-sulphur-containing poly(hydroxycarboxylic acid) amide salt derivatives.
  • The preparation of poly(hydroxycarboxylic acid) and its amide or other derivatives is known and is described, for instance, in EP 0 164 817, WO 95/17473, WO 96/07689, U.S. Pat. No. 5,536,445, GB 2 001 083, GB 1 342 746, GB 1 373 660, U.S. Pat. No. 5,000,792 and U.S. Pat. No. 4,349,389 which disclosures are herein incorporated by reference.
  • The poly(hydroxycarboxylic acid)s of formula (I) may be made by the interesterification of one or more hydroxycarboxylic acids of formula (II)

  • HO-A-COOH  (II)
  • wherein A is a divalent optionally substituted hydrocarbyl group, optionally in the presence of a catalyst according to well known methods. Such methods are described, for example, in U.S. Pat. No. 3,996,059, GB 1 373 660 and GB 1 342 746.
  • The chain terminator in said interesterification may be a non-hydroxycarboxylic acid.
  • The hydroxyl group in the hydroxycarboxylic acid and the carboxylic acid group in the hydroxycarboxylic acid or the non-hydroxycarboxylic acid may be primary, secondary or tertiary in character.
  • The interesterification of the hydroxycarboxylic acid and the non-hydroxycarboxylic acid chain terminator may be effected by heating the starting materials, optionally in a suitable hydrocarbon solvent such as toluene or xylene, and azeotroping off the formed water. The reaction may be carried out at a temperature up to −250° C., conveniently at the reflux temperature of the solvent.
  • Where the hydroxyl group in the hydroxycarboxylic acid is secondary or tertiary, the temperature employed should not be so high as to lead to dehydration of the acid molecule.
  • Catalysts for the interesterification, such as p-toluenesulphonic acid, zinc acetate, zirconium naphthenate or tetrabutyl titanate, may be included, with the objective of either increasing the rate of reaction at a given temperature or of reducing the temperature required for a given rate of reaction.
  • In the compounds of formulae (I) and (II), A is preferably an optionally substituted aromatic, aliphatic or cycloaliphatic straight chain or branched divalent hydrocarbyl group. Preferably, A is an arylene, alkylene or alkenylene group, in particular an arylene, alkylene or alkenylene group containing in the range of from 4 to 25 carbon atoms, more preferably in the range of from 6 to 25 carbon atoms, more preferably in the range of from 8 to 24 carbon atoms, more preferably in the range of from 10 to 22 carbon atoms, and most preferably in the range of from 12 to 20 carbon atoms.
  • Preferably, in said compounds of formulae (I) and (II), there are at least 4 carbon atoms, more preferably at least 6 carbon atoms, and even more preferably in the range of from 8 to 14 carbon atoms connected directly between the carbonyl group and the oxygen atom derived from the hydroxyl group.
  • In the compounds of formulae (I) and (II), the optional substituents in the group A are preferably selected from hydroxy, halo or alkoxy groups, more preferably C1-4 alkoxy groups.
  • The hydroxyl group in the hydroxycarboxylic acids of formula (II) is preferably a secondary hydroxyl group.
  • Examples of suitable hydroxycarboxylic acids are 9-hydroxystearic acid, 10-hydroxystearic acid, 12-hydroxystearic acid, 12-hydroxy-9-oleic acid (ricinoleic acid), 6-hydroxycaproic acid, preferably 12-hydroxystearic acid. Commercial 12-hydroxystearic acid (hydrogenated castor oil fatty acid) normally contains up to 15% wt of stearic acid and other non-hydroxycarboxylic acids as impurities and can conveniently be used without further admixture to produce a polymer of molecular weight about 1000-2000.
  • Where the non-hydroxycarboxylic acid is introduced separately to the reaction, the proportion which is required in order to produce a polymer or oligomer of a given molecular weight can be determined either by simple experiment or by calculation by the person skilled in the art.
  • The group (—O-A-CO—) in the compounds of formulae (I) and (II) is preferably a 12-oxystearyl group, 12-oxyoleyl group or a 6-oxycaproyl group.
  • Preferred poly(hydroxycarboxylic acid)s of formula (I) for reaction with amine include poly(hydroxystearic acid) and poly(hydroxyoleic acid).
  • The amines which react with poly(hydroxycarboxylic acid)s of formula (I) to form poly(hydroxycarboxylic acid) amide intermediates may include those defined in WO 97/41092.
  • For example, various amines and their preparations are described in U.S. Pat. No. 3,275,554, U.S. Pat. No. 3,438,757, U.S. Pat. No. 3,454,555, U.S. Pat. No. 3,565,804, U.S. Pat. No. 3,755,433 and U.S. Pat. No. 3,822,209 which disclosures are herein incorporated by reference.
  • The amine reactant is preferably a diamine, a triamine or a polyamine.
  • Preferred amine reactants are diamines selected from ethylenediamine, N,N-dimethyl-1,3-propanediamine, triamines and polyamines selected from dietheylenetriamine, triethylenetetramine, tetraethylenepentamine, pentaethylenehexamine and tris(2-aminoethyl)amine.
  • The amidation between the amine reactant and the (poly(hydroxycarboxylic acid) of formula (I) may be carried out according to methods known to those skilled in the art, by heating the poly(hydroxycarboxylic acid) with the amine reactant, optionally in a suitable hydrocarbon solvent such as toluene or xylene, and azeotroping off the formed water. Said reaction may be carried out in the presence of a catalyst such as p-toluenesulphonic acid, zinc acetate, zirconium naphthenate or tetrabutyl titanate.
  • Various patent documents disclose poly(hydroxycarboxylic acid) amide derivatives.
  • For instance, GB 1 373 660 discloses poly(hydroxycarboxylic acid) amide derivatives with amines such as 3-dimethylaminopropylamine and ethylenediamine for use as dispersing agents in dispersions of pigments in organic liquids.
  • GB 2 001 083 discloses poly(hydroxycarboxylic acid) amide derivatives with poly(ethyleneimine) (PEI) having a molecular weight (MW) greater than 500 for a similar use.
  • In U.S. Pat. No. 5,000,792, poly(hydroxycarboxylic acid) amide derivatives with amines of the formula of NH2−R′—N(R″)—R′″—NH2 are disclosed for use as pigment dispersing agent.
  • WO 95/17473 discloses poly(hydroxycarboxylic acid) amide derivatives with amines such as 3-dimethylaminopropylamine, ethylenediamine, poly(ethyleneimine) (PEI) having a molecular weight (MW) greater than 500 and amines of the formula of NH2R′—N(R″)—R′″—NH2 for use in a method of preparing a non-aqueous dispersion of copper phthalocyanine.
  • U.S. Pat. No. 4,349,389 discloses poly(hydroxycarboxylic acid) amide derivatives with amines such as 3-dimethyl-aminopropylamine, poly(ethyleneimine) (PEI) having a molecular weight (MW) greater than 500 as dispersing agent in the preparation of a dispersible inorganic pigment composition.
  • EP 0 164 817 discloses poly(hydroxycarboxylic acid) amide derivatives with polyamines (ethylenediamine, diethylenetriamine, etc.), aminoalcohols (diethanolamine, etc.) and ester derivatives with polyols (glycerol, etc.) for use as surfactant suitable for stabilising dispersions of solids in organic liquids and oil/water emulsions.
  • However, none of the afore-mentioned patent documents disclose the use of one or more poly(hydroxycarboxylic acid) amide salt derivatives as disclosed herein in fuel compositions.
  • The poly(hydroxycarboxylic acid) amide intermediate formed from reaction of the amine and the poly(hydroxycarboxylic acid) of formula (I) is reacted with an acid or a quaternizing agent to form a salt derivative, according to well-known methods.
  • Acids that may be used to form the salt derivative may be selected from organic or inorganic acids. Said acids are conveniently selected from carboxylic acids, nitrogen-containing organic and inorganic acids, sulphur-containing organic or inorganic acids (such as sulphuric acid, methanesulphonic acid and benzenesulphonic acid).
  • Quaternizing agents that may be used to form the salt derivative may be selected from dimethylsulphuric acid, a dialkyl sulphate having from 1 to 4 carbon atoms, an alkyl halide such as methyl chloride, methyl bromide, aryl halide such as benzyl chloride.
  • In a preferred embodiment, the quaternizing agent is a sulphur-containing quaternizing agent, in particular dimethylsulphuric acid or an dialkyl sulphate having from 1 to 4 carbon atoms. The quaternizing agent is preferably dimethyl sulphate.
  • Quaternization is a well-known method in the art. For example, quaternization using dimethyl sulphate is described in U.S. Pat. No. 3,996,059, U.S. Pat. No. 4,349,389 and GB 1 373 660.
  • Poly(hydroxycarboxylic acid) amide salt derivatives that are preferred in the present invention are those which each have a TBN (total base number) value of less than 10 mg·KOH/g, as measured by ASTM D 4739. More preferably, the poly(hydroxycarboxylic acid) amide salt derivatives each have a TBN value of less than 5 mg·KOH/g, most preferably 2 mg·KOH/g or less, as measured by ASTM D 4739.
  • Examples of poly(hydroxycarboxylic acid) amide salt derivatives that are available commercially include that available from Lubrizol under the trade designation “SOLSPERSE 17000” (a reaction product of poly(12-hydroxystearic acid) with N,N-dimethyl-1,3-propanediamine and dimethyl sulphate) and those available under the trade designations “CH-5” and “CH-7” from Shanghai Sanzheng Polymer Company.
  • In the liquid fuel compositions of the present invention, if the base fuel used is a gasoline, then the gasoline may be any gasoline suitable for use in an internal combustion engine of the spark-ignition (petrol) type known in the art. The gasoline used as the base fuel in the liquid fuel composition of the present invention may conveniently also be referred to as ‘base gasoline’.
  • Gasolines typically comprise mixtures of hydrocarbons boiling in the range from 25 to 230° C. (EN-ISO 3405), the optimal ranges and distillation curves typically varying according to climate and season of the year. The hydrocarbons in a gasoline may be derived by any means known in the art, conveniently the hydrocarbons may be derived in any known manner from straight-run gasoline, synthetically-produced aromatic hydrocarbon mixtures, thermally or catalytically cracked hydrocarbons, hydro-cracked petroleum fractions, catalytically reformed hydrocarbons or mixtures of these.
  • The specific distillation curve, hydrocarbon composition, research octane number (RON) and motor octane number (MON) of the gasoline are not critical.
  • Conveniently, the research octane number (RON) of the gasoline may be at least 80, for instance in the range of from 80 to 110, preferably the RON of the gasoline will be at least 90, for instance in the range of from 90 to 110, more preferably the RON of the gasoline will be at least 91, for instance in the range of from 91 to 105, even more preferably the RON of the gasoline will be at least 92, for instance in the range of from 92 to 103, even more preferably the RON of the gasoline will be at least 93, for instance in the range of from 93 to 102, and most preferably the RON of the gasoline will be at least 94, for instance in the range of from 94 to 100 (EN 25164); the motor octane number (MON) of the gasoline may conveniently be at least 70, for instance in the range of from 70 to 110, preferably the MON of the gasoline will be at least 75, for instance in the range of from 75 to 105, more preferably the MON of the gasoline will be at least 80, for instance in the range of from 80 to 100, most preferably the MON of the gasoline will be at least 82, for instance in the range of from 82 to 95 (EN 25163).
  • Typically, gasolines comprise components selected from one or more of the following groups; saturated hydrocarbons, olefinic hydrocarbons, aromatic hydrocarbons, and oxygenated hydrocarbons. Conveniently, the gasoline may comprise a mixture of saturated hydrocarbons, olefinic hydrocarbons, aromatic hydrocarbons, and, optionally, oxygenated hydrocarbons.
  • Typically, the olefinic hydrocarbon content of the gasoline is in the range of from 0 to 40 percent by volume based on the gasoline (ASTM D1319); preferably, the olefinic hydrocarbon content of the gasoline is in the range of from 0 to 30 percent by volume based on the gasoline, more preferably, the olefinic hydrocarbon content of the gasoline is in the range of from 0 to 20 percent by volume based on the gasoline.
  • Typically, the aromatic hydrocarbon content of the gasoline is in the range of from 0 to 70 percent by volume based on the gasoline (ASTM D1319), for instance the aromatic hydrocarbon content of the gasoline is in the range of from 10 to 60 percent by volume based on the gasoline; preferably, the aromatic hydrocarbon content of the gasoline is in the range of from 0 to 50 percent by volume based on the gasoline, for instance the aromatic hydrocarbon content of the gasoline is in the range of from 10 to 50 percent by volume based on the gasoline.
  • The benzene content of the gasoline is at most 10 percent by volume, more preferably at most 5 percent by volume, especially at most 1 percent by volume based on the gasoline.
  • The gasoline preferably has a low or ultra low sulphur content, for instance at most 1000 ppmw (parts per million by weight), preferably no more than 500 ppmw, more preferably no more than 100, even more preferably no more than 50 and most preferably no more than even 10 ppmw.
  • The gasoline also preferably has a low total lead content, such as at most 0.005 g/l, most preferably being lead free—having no lead compounds added thereto (i.e. unleaded).
  • When the gasoline comprises oxygenated hydrocarbons, at least a portion of non-oxygenated hydrocarbons will be substituted for oxygenated hydrocarbons. The oxygen content of the gasoline may be up to 35 percent by weight (EN 1601) (e.g. ethanol per se) based on the gasoline. For example, the oxygen content of the gasoline may be up to 25 percent by weight, preferably up to 10 percent by weight. Conveniently, the oxygenate concentration will have a minimum concentration selected from any one of 0, 0.2, 0.4, 0.6, 0.8, 1.0, and 1.2 percent by weight, and a maximum concentration selected from any one of 5, 4.5, 4.0, 3.5, 3.0, and 2.7 percent by weight.
  • Examples of oxygenated hydrocarbons that may be incorporated into the gasoline include alcohols, ethers, esters, ketones, aldehydes, carboxylic acids and their derivatives, and oxygen containing heterocyclic compounds. Preferably, the oxygenated hydrocarbons that may be incorporated into the gasoline are selected from alcohols (such as methanol, ethanol, propanol, iso-propanol, butanol, tert-butanol and iso-butanol), ethers (preferably ethers containing 5 or more carbon atoms per molecule, e.g., methyl tert-butyl ether) and esters (preferably esters containing 5 or more carbon atoms per molecule); a particularly preferred oxygenated hydrocarbon is ethanol.
  • When oxygenated hydrocarbons are present in the gasoline, the amount of oxygenated hydrocarbons in the gasoline may vary over a wide range. For example, gasolines comprising a major proportion of oxygenated hydrocarbons are currently commercially available in countries such as Brazil and U.S.A, e.g. ethanol per se and E85, as well as gasolines comprising a minor proportion of oxygenated hydrocarbons, e.g. E10 and E5. Therefore, the gasoline may contain up to 100 percent by volume oxygenated hydrocarbons. Preferably, the amount of oxygenated hydrocarbons present in the gasoline is selected from one of the following amounts: up to 85 percent by volume; up to 65 percent by volume; up to 30 percent by volume; up to 20 percent by volume; up to 15 percent by volume; and, up to 10 percent by volume, depending upon the desired final formulation of the gasoline. Conveniently, the gasoline may contain at least 0.5, 1.0 or 2.0 percent by volume oxygenated hydrocarbons.
  • Examples of suitable gasolines include gasolines which have an olefinic hydrocarbon content of from 0 to 20 percent by volume (ASTM D1319), an oxygen content of from 0 to 5 percent by weight (EN 1601), an aromatic hydrocarbon content of from 0 to 50 percent by volume (ASTM D1319) and a benzene content of at most 1 percent by volume.
  • Whilst not critical to the present invention, the base gasoline or the gasoline composition of the present invention may conveniently additionally include one or more fuel additive. The concentration and nature of the fuel additive(s) that may be included in the base gasoline or the gasoline composition of the present invention is not critical. Non-limiting examples of suitable types of fuel additives that can be included in the base gasoline or the gasoline composition of the present invention include anti-oxidants, corrosion inhibitors, detergents, dehazers, antiknock additives, metal deactivators, valve-seat recession protectant compounds, dyes, friction modifiers, carrier fluids, diluents and markers. Examples of suitable such additives are described generally in U.S. Pat. No. 5,855,629.
  • Conveniently, the fuel additives can be blended with one or more diluents or carrier fluids, to form an additive concentrate, the additive concentrate can then be admixed with the base gasoline or the gasoline composition of the present invention.
  • The (active matter) concentration of any additives present in the base gasoline or the gasoline composition of the present invention is preferably up to 1 percent by weight, more preferably in the range from 5 to 1000 ppmw, advantageously in the range of from 75 to 300 ppmw, such as from 95 to 150 ppmw.
  • In the liquid fuel compositions of the present invention, if the base fuel used is a diesel fuel, then the diesel fuel used as the base fuel in the present invention includes diesel fuels for use in automotive compression ignition engines, as well as in other types of engine such as for example marine, railroad and stationary engines. The diesel fuel used as the base fuel in the liquid fuel composition of the present invention may conveniently also be referred to as ‘diesel base fuel’.
  • The diesel base fuel may itself comprise a mixture of two or more different diesel fuel components, and/or be additivated as described below.
  • Such diesel fuels will contain one or more base fuels which may typically comprise liquid hydrocarbon middle distillate gas oil(s), for instance petroleum derived gas oils. Such fuels will typically have boiling points within the usual diesel range of 150 to 400° C., depending on grade and use. They will typically have a density from 750 to 1000 kg/m3, preferably from 780 to 860 kg/m3, at 15° C. (e.g. ASTM D4502 or IP 365) and a cetane number (ASTM D613) of from 35 to 120, more preferably from 40 to 85. They will typically have an initial boiling point in the range 150 to 230° C. and a final boiling point in the range 290 to 400° C. Their kinematic viscosity at 40° C. (ASTM D445) might suitably be from 1.2 to 4.5 mm2/s.
  • An example of a petroleum derived gas oil is a Swedish Class 1 base fuel, which will have a density from 800 to 820 kg/m3 at 15° C. (SS-EN ISO 3675, SS-EN ISO 12185), a T95 of 320° C. or less (SS-EN ISO 3405) and a kinematic viscosity at 40° C. (SS-EN ISO 3104) from 1.4 to 4.0 mm2/s, as defined by the Swedish national specification EC1.
  • Optionally, non-mineral oil based fuels, such as biofuels or Fischer-Tropsch derived fuels, may also form or be present in the diesel fuel. Such Fischer-Tropsch fuels may for example be derived from natural gas, natural gas liquids, petroleum or shale oil, petroleum or shale oil processing residues, coal or biomass.
  • The amount of Fischer-Tropsch derived fuel used in the diesel fuel may be from 0% to 100% v of the overall diesel fuel, preferably from 5% to 100% v, more preferably from 5% to 75% v. It may be desirable for such a diesel fuel to contain 10% v or greater, more preferably 20% v or greater, still more preferably 30% v or greater, of the Fischer-Tropsch derived fuel. It is particularly preferred for such diesel fuels to contain 30 to 75% v, and particularly 30 or 70% v, of the Fischer-Tropsch derived fuel. The balance of the diesel fuel is made up of one or more other diesel fuel components.
  • Such a Fischer-Tropsch derived fuel component is any fraction of the middle distillate fuel range, which can be isolated from the (optionally hydrocracked) Fischer-Tropsch synthesis product. Typical fractions will boil in the naphtha, kerosene or gas oil range. Preferably, a Fischer-Tropsch product boiling in the kerosene or gas oil range is used because these products are easier to handle in for example domestic environments. Such products will suitably comprise a fraction larger than 90 wt % which boils between 160 and 400° C., preferably to about 370° C. Examples of Fischer-Tropsch derived kerosene and gas oils are described in EP-A-0583836, WO-A-97/14768, WO-A-97/14769, WO-A-00/11116, WO-A-00/11117, WO-A-01/83406, WO-A-01/83648, WO-A-01/83647, WO-A-01/83641, WO-A-00/20535, WO-A-00/20534, EP-A-1101813, U.S. Pat. No. 5,766,274, U.S. Pat. No. 5,378,348, U.S. Pat. No. 5,888,376 and U.S. Pat. No. 6,204,426 which disclosures are herein incorporated by reference.
  • The Fischer-Tropsch product will suitably contain more than about 80 wt % and more suitably more than about 95 wt % iso and normal paraffins and less than about 1 wt % aromatics, the balance being naphthenics compounds. The content of sulphur and nitrogen will be very low and normally below the detection limits for such compounds. For this reason the sulphur content of a diesel fuel composition containing a Fischer-Tropsch product may be very low.
  • The diesel fuel composition preferably contains no more than 5000 ppmw sulphur, more preferably no more than 500 ppmw, or no more than 350 ppmw, or no more than 150 ppmw, or no more than 100 ppmw, or no more than 70 ppmw, or no more than 50 ppmw, or no more than 30 ppmw, or no more than 20 ppmw, or most preferably no more than 15 ppmw sulphur.
  • The diesel base fuel may itself be additivated (additive-containing) or unadditivated (additive-free). If additivated, e.g. at the refinery, it will contain minor amounts of one or more additives selected for example from anti-static agents, pipeline drag reducers, flow improvers (e.g. ethylene/vinyl acetate copolymers or acrylate/maleic anhydride copolymers), lubricity additives, antioxidants and wax anti-settling agents.
  • Detergent-containing diesel fuel additives are known and commercially available. Such additives may be added to diesel fuels at levels intended to reduce, remove, or slow the build up of engine deposits.
  • Examples of detergents suitable for use in diesel fuel additives for the present purpose include polyolefin substituted succinimides or succinamides of polyamines, for instance polyisobutylene succinimides or polyisobutylene amine succinamides, aliphatic amines, Mannich bases or amines and polyolefin (e.g. polyisobutylene) maleic anhydrides. Succinimide dispersant additives are described for example in GB-A-960493, EP-A-0147240, EP-A-0482253, EP-A-0613938, EP-A-0557516 and WO-A-98/42808. Particularly preferred are polyolefin substituted succinimides such as polyisobutylene succinimides.
  • The diesel fuel additive mixture may contain other components in addition to the detergent. Examples are lubricity enhancers; dehazers, e.g. alkoxylated phenol formaldehyde polymers; anti-foaming agents (e.g. polyether-modified polysiloxanes); ignition improvers (cetane improvers) (e.g. 2-ethylhexyl nitrate (EHN), cyclohexyl nitrate, di-tert-butyl peroxide and those disclosed in U.S. Pat. No. 4,208,190 at column 2, line 27 to column 3, line 21) which disclosure is herein incorporated by reference; anti-rust agents (e.g. a propane-1,2-diol semi-ester of tetrapropenyl succinic acid, or polyhydric alcohol esters of a succinic acid derivative, the succinic acid derivative having on at least one of its alpha-carbon atoms an unsubstituted or substituted aliphatic hydrocarbon group containing from 20 to 500 carbon atoms, e.g. the pentaerythritol diester of polyisobutylene-substituted succinic acid); corrosion inhibitors; reodorants; anti-wear additives; anti-oxidants (e.g. phenolics such as 2,6-di-tert-butylphenol, or phenylenediamines such as N,N′-di-sec-butyl-p-phenylenediamine); metal deactivators; combustion improvers; static dissipator additives; cold flow improvers; and wax anti-settling agents.
  • The diesel fuel additive mixture may contain a lubricity enhancer, especially when the diesel fuel composition has a low (e.g. 500 ppmw or less) sulphur content. In the additivated diesel fuel composition, the lubricity enhancer is conveniently present at a concentration of less than 1000 ppmw, preferably between 50 and 1000 ppmw, more preferably between 70 and 1000 ppmw. Suitable commercially available lubricity enhancers include ester- and acid-based additives. Other lubricity enhancers are described in the patent literature, in particular in connection with their use in low sulphur content diesel fuels, for example in:
      • the paper by Danping Wei and H. A. Spikes, “The Lubricity of Diesel Fuels”, Wear, III (1986) 217-235;
      • WO-A-95/33805—cold flow improvers to enhance lubricity of low sulphur fuels;
      • WO-A-94/17160—certain esters of a carboxylic acid and an alcohol wherein the acid has from 2 to 50 carbon atoms and the alcohol has 1 or more carbon atoms, particularly glycerol monooleate and di-isodecyl adipate, as fuel additives for wear reduction in a diesel engine injection system;
      • U.S. Pat. No. 5,490,864—certain dithiophosphoric diester-dialcohols as anti-wear lubricity additives for low sulphur diesel fuels; and
      • WO-A-98/01516—certain alkyl aromatic compounds having at least one carboxyl group attached to their aromatic nuclei, to confer anti-wear lubricity effects particularly in low sulphur diesel fuels.
  • It may also be preferred for the diesel fuel composition to contain an anti-foaming agent, more preferably in combination with an anti-rust agent and/or a corrosion inhibitor and/or a lubricity enhancing additive.
  • Unless otherwise stated, the (active matter) concentration of each such additive component in the additivated diesel fuel composition is preferably up to 10000 ppmw, more preferably in the range from 0.1 to 1000 ppmw, advantageously from 0.1 to 300 ppmw, such as from 0.1 to 150 ppmw.
  • The (active matter) concentration of any dehazer in the diesel fuel composition will preferably be in the range from 0.1 to 20 ppmw, more preferably from 1 to 15 ppmw, still more preferably from 1 to 10 ppmw, advantageously from 1 to 5 ppmw. The (active matter) concentration of any ignition improver present will preferably be 2600 ppmw or less, more preferably 2000 ppmw or less, conveniently from 300 to 1500 ppmw. The (active matter) concentration of any detergent in the diesel fuel composition will preferably be in the range from 5 to 1500 ppmw, more preferably from 10 to 750 ppmw, most preferably from 20 to 500 ppmw.
  • In the case of a diesel fuel composition, for example, the fuel additive mixture will typically contain a detergent, optionally together with other components as described above, and a diesel fuel-compatible diluent, which may be a mineral oil, a solvent such as those sold by Shell companies under the trade mark “SHELLSOL”, a polar solvent such as an ester and, in particular, an alcohol, e.g. hexanol, 2-ethylhexanol, decanol, isotridecanol and alcohol mixtures such as those sold by Shell companies under the trade mark “LINEVOL”, especially LINEVOL 79 alcohol which is a mixture of C7-9 primary alcohols, or a C12-14 alcohol mixture which is commercially available.
  • The total content of the additives in the diesel fuel composition may be suitably between 0 and 10000 ppmw and preferably below 5000 ppmw.
  • In the above, amounts (concentrations, % vol, ppmw, % wt) of components are of active matter, i.e. exclusive of volatile solvents/diluent materials.
  • The liquid fuel composition of the present invention is produced by admixing the one or more poly(hydroxycarboxylic acid) amide salt derivatives with a base fuel suitable for use in an internal combustion engine. If the base fuel to which the one or more poly(hydroxycarboxylic acid) amide salt derivatives is admixed is a gasoline, then the liquid fuel composition produced is a gasoline composition; likewise, if the base fuel to which the one or more poly(hydroxycarboxylic acid) amide salt derivatives is admixed is a diesel fuel, then the liquid fuel composition produced is a diesel fuel composition.
  • Preferably, the amount of the one or more poly(hydroxycarboxylic acid) amide salt derivatives present in the liquid fuel composition of the present invention is at least 1 ppmw (part per million by weight), based on the overall weight of the liquid fuel composition. More preferably, the amount of the one or more poly(hydroxycarboxylic acid) amide salt derivatives present in the liquid fuel composition of the present invention additionally accords with one or more of the parameters (i) to (xx) listed below:
  • (i) at least 10 ppmw
    (ii) at least 20 ppmw
    (iii) at least 30 ppmw
    (iv) at least 40 ppmw
    (v) at least 50 ppmw
    (vi) at least 60 ppmw
    (vii) at least 70 ppmw
    (viii) at least 80 ppmw
    (ix) at least 90 ppmw
    (x) at least 100 ppmw
    (xi) at most 20% wt.
    (xii) at most 18% wt.
    (xiii) at most 16% wt.
    (xiv) at most 14% wt.
    (xv) at most 12% wt.
    (xvi) at most 10% wt.
    (xvii) at most 8% wt.
    (xviii) at most 6% wt.
    (xix) at most 4% wt.
    (xx) at most 2% wt.
  • Conveniently, the amount of the one or more poly(hydroxycarboxylic acid) amide salt derivatives present in the liquid fuel composition of the present invention may also be at least 200 ppmw, at least 300 ppmw, at least 400 ppmw, at least 500 ppmw, or even at least 1000 ppmw.
  • It has been found that the use of the one or more poly(hydroxycarboxylic acid) amide salt derivatives in the liquid fuel compositions can provide significant benefits in terms of improved lubricity of the liquid fuel composition, in particular when the liquid fuel composition is gasoline, relative to the liquid base fuel.
  • By the term “improved/improving lubricity” used herein, it is meant that the wear scar produced using a high frequency reciprocating rig (HFRR) is reduced.
  • It has additionally been found that the use of the one or more poly(hydroxycarboxylic acid) amide salt derivatives in liquid fuel compositions can also provide benefits in terms of engine cleanliness, in particular in terms of improved inlet valve deposit keep clean and/or injector nozzle keep clean performance, of an internal combustion engine being fuelled by the liquid fuel composition of the present invention relative to the internal combustion engine being fuelled by the liquid base fuel.
  • By the term “improved/improving inlet valve deposit keep clean performance”, it is meant that the weight of deposit formed on the inlet valve of the engine is reduced relative to the base fuel not containing the one or more poly(hydroxycarboxylic acid) amide salt derivatives.
  • By the term “improved/improving injector nozzle keep clean performance”, it is meant that the amount of deposit formed on the injector nozzle of the engine is reduced as measured by the loss of engine torque.
  • It has additionally been found that the use of the one or more poly(hydroxycarboxylic acid) amide salt derivatives in liquid fuel compositions can also provide benefits in terms improved fuel economy of an internal combustion engine being fuelled by the liquid fuel composition of the present invention relative to the internal combustion engine being fuelled by the liquid base fuel.
  • The present invention therefore also provides a method of improving the lubricity of a liquid base fuel suitable for use in an internal combustion engine, comprising admixing one or more poly(hydroxycarboxylic acid) amide salt derivatives with a major portion of the liquid base fuel suitable for use in an internal combustion engine; a method of improving the inlet valve deposit clean up performance of a liquid base fuel suitable for use in an internal combustion engine, comprising admixing one or more poly(hydroxycarboxylic acid) amide salt derivatives with a major portion of the liquid base fuel suitable for use in an internal combustion engine; a method of improving the injector nozzle keep clean performance of a liquid base fuel suitable for use in an internal combustion engine, comprising admixing one or more poly(hydroxycarboxylic acid) amide salt derivatives with a major portion of the liquid base fuel suitable for use in an internal combustion engine; and, a method of improving the fuel economy performance of a liquid base fuel suitable for use in an internal combustion engine, comprising admixing one or more poly(hydroxycarboxylic acid) amide salt derivatives with a major portion of the liquid base fuel suitable for use in an internal combustion engine.
  • It has additionally been found that the use of the one or more poly(hydroxycarboxylic acid) amide salt derivatives in liquid fuel compositions can also provide benefits in terms improving the lubricant performance of an internal combustion engine being fuelled by the liquid fuel composition of the present invention relative to the internal combustion engine being fuelled by the liquid base fuel.
  • In particular, the improvement in the lubricant performance of the internal combustion engine fuelled by a liquid fuel composition according to the present invention can be observed by the a reduction in the levels of sludge and varnish on specific engine parts, such as sludge on rocker arm covers, cam baffles, timing chain covers, oil pans, oil pan baffles, and valve decks, and varnish on piston skirts and cam baffles.
  • In particular, it has been found that the use of the one or more poly(hydroxycarboxylic acid) amide salt derivatives in a gasoline compositions can provide benefits in terms inhibiting specific sludge and varnish deposit formation, as measured by ASTM D 6593-07, of an internal combustion engine being fuelled by the gasoline composition of the present invention relative to the internal combustion engine being fuelled by the gasoline base fuel.
  • Therefore, the present invention also provides a method of improving the performance of the lubricant of an internal combustion engine, said method comprising fuelling an internal combustion engine containing the engine lubricant with a liquid fuel composition according to the present invention.
  • It has also been observed that the use of one or more poly(hydroxycarboxylic acid) amide salt derivatives wherein the anion is a non-sulfur-containing anion in a liquid fuel composition can have the additional advantage of improved phosphorus volatility properties of the engine lubricant of an internal combustion engine fuelled by the liquid fuel composition compared to the phosphorus volatility properties of the engine lubricant when one or more poly(hydroxycarboxylic acid) amide salt derivatives wherein the anion is a sulfur-containing anion is used in the liquid fuel composition.
  • The phosphorus volatility properties of the engine lubricant can conveniently be measured according to the phosphorus emission index (PEI) test, which is also known as the “Selby-Noack PEI test”. This test has been described in T. W. Selby, R. J. Bosch and D.C. Fee, “Continued Studies of the Causes of Engine Oil, Phosphorus Volatility—Part 2”. SAE 2007-01-1073, the teaching of which is hereby incorporated by specific reference. The “Selby-Noack PEI test” is similar to the “Noack procedure” as described in ASTM D 5800, procedure C, but deviates in duration (16 hours instead of 24 hours for the Noack procedure) and temperature (250° C. for the Noack procedure). As the PEI is an approximation of the quantity of phosphorus (mg) obtained from 1 kg of fluid, it has no unit. By the term “improved phosphorus volatility properties”, it is meant that the PEI is lower than the PEI result it is being compared to.
  • Therefore, the present invention also provides the use of one or more poly(hydroxycarboxylic acid) amide salt derivatives wherein the anion is a non-sulfur-containing anion in a liquid fuel composition according to the present invention for improving the phosphorus volatility properties of an engine lubricant of an internal combustion engine fuelled by the liquid fuel composition compared to the phosphorus volatility properties of the engine lubricant when one or more poly(hydroxycarboxylic acid) amide salt derivatives wherein the anion is a sulfur-containing anion is used in the liquid fuel composition.
  • The present invention further provides a method of operating an internal combustion engine, which method involves introducing into a combustion chamber of the engine a liquid fuel composition according to the present invention.
  • The one or more poly(hydroxycarboxylic acid) amide salt derivatives of the present invention may also be conveniently incorporated into lubricant formulations, especially engine crank case lubricant formulations.
  • The present invention will be further understood from the following examples. Unless otherwise stated, all amounts and concentrations disclosed in the examples are based on weight of the fully formulated fuel composition. The examples are provided for illustration only and are not to be construed as limiting the claimed invention in any way.
  • EXAMPLES
  • In examples 1 to 41, two different commercially available hyperdispersants have been used, the hyperdispersants were poly(hydroxycarboxylic acid) amide salt derivatives, wherein the anion is a methyl sulphate anion, according to the present invention were products available commercially from Shanghai Sanzheng Polymer Company under the trade designations “CH-5” and “CH-7”. Certain measured properties of both CH-5 and CH-7 are given in Table 1 below:
  • TABLE 1
    Measure properties of CH-5 and CH-7
    MW TBN (mgKOH/g) (ASTM D 4739) N (% w) S (% w)
    CH-5 ~1130 1.9 0.89 0.95
    CH-7 ~1050 1.9 0.82 0.86
  • Examples 1 to 39 and Comparative Examples A to D
  • The CH-5 and CH-7 hyperdispersants described above were blended into a base fuel selected from the gasoline, diesel, GTL diesel and Swedish Class I diesel base fuels described in Tables 2 and 3 below, in various amounts.
  • TABLE 2
    Diesel base fuels.
    Parameter Diesel A Diesel Ba Diesel Cb
    Cetane No. 52.80 >76 53.10
    (ASTM D613)
    Density at 0.84 g/cm3 0.78 g/cm3 0.82 g/cm3
    15° C. (IP365)
    Flash Point 62.0° C. 104.0° C. 72.5° C.
    (IP34)
    IBP (IP123) 168.6° C. 211.0° C. 190.3° C.
    10% rec. 201.3° C. 251.3° C. 203.4° C.
    (IP123)
    20% rec. 223.9° C. 262.4° C. 211.1° C.
    (IP123)
    30% rec. 246.3° C. 273.3° C. 225.9° C.
    (IP123)
    40% rec. 266.7° C. 285.6° C. 225.9° C.
    (IP123)
    50% rec. 281.8° C. 297.3° C. 234.2° C.
    (IP123)
    60% rec. 293.9° C. 307.6° C. 242.2° C.
    (IP123)
    70% rec. 306.0° C. 316.9° C. 250.6° C.
    (IP123)
    80% rec. 319.7° C. 326.9° C. 259.4° C.
    (IP123)
    90% rec. 337.2° C. 339.1° C. 270.5° C.
    (IP123)
    95% rec. 350.8° C. 348.6° C. 279.5° C.
    (IP123)
    FBP (IP123) 362.3° C. 355.3° C. 291.6° C.
    Viscosity at 2.74 mm2/s 3.54 mm2/s 1.94 mm2/s
    40° C. (IP71)
    Sulphur content 8.4 mg/kgc <3 mg/kgc <3 mg/kgd
    Total 40.5% m/m 0.4% m/m 13.3% m/m
    Aromatics
    (IP391/01/
    IP548/07)
    aFischer-Tropsch (GTL) derived diesel fuel
    bSwedish Class I diesel fuel
    cISO 20884
    dISO 20846
  • TABLE 3
    Gasoline base fuel.
    Parameter “Gasoline”
    RON (ASTM D2699) 96.00
    MON (ASTM D2700) 85.10
    Density at 15° C. (IP365) 0.73 g/cm3
    IBP (IP123) 26.5° C.
    10% rec. (IP123) 37.9° C.
    20% rec. (IP123) 48.9° C.
    30% rec. (IP123) 61.0° C.
    40% rec. (IP123) 74.4° C.
    50% rec. (IP123) 88.2° C.
    60% rec. (IP123) 101.4° C.
    70% rec. (IP123) 113.3° C.
    80% rec. (IP123) 127.9° C.
    90% rec. (IP123) 149.2° C.
    95% rec. (IP123) 164.7° C.
    FBP (IP123) 191.2° C.
    RVP *(IP394) 87.8 kPa
    Olefins (inc. dienes) 16.40% vol.
    Aromatics 28.88% vol.
  • To assess the lubricity of the liquid fuel compositions described above, the following test procedures were used.
  • The lubricity of the diesel fuel compositions was determined using the HFRR test used described in ISO 12156-1.
  • The lubricity of the gasoline compositions was determined by using a modified HFRR test. The modified HFRR test is based on ISO 12156-1 using a PCS Instruments HFRR supplemented with the PCS Instruments Gasoline Conversion Kit, and using a fluid volume of 15.0 ml (+/−0.2 ml), a fluid temperature of 25.0° C. (+/−1° C.), and wherein a PTFE cover is used to cover the test sample in order to minimise evaporation.
  • The results of the lubricity tests are given below in Table 4.
  • TABLE 4
    HFRR Results for base fuel and fuel compositions
    according to the present invention.
    Hyperdispersant Average HFRR
    Example Base Fuel (concentration) Wear Scar (μm)
    A* Diesel A 366.5
     1 Diesel A CH-5 (100 ppmw) 344.5
     2 Diesel A CH-5 (500 ppmw) 341.5
     3 Diesel A CH-5 (1000 ppmw) 332
     4 Diesel A CH-5 (1% wt) 254
     5 Diesel A CH-5 (10% wt.) 224.5
     6 Diesel A CH-7 (50 ppmw) 319.5
     7 Diesel A CH-7 (100 ppmw) 321.5
     8 Diesel A CH-7 (500 ppmw) 327.5
     9 Diesel A CH-7 (1000 ppmw) 322
    10 Diesel A CH-7 (1% wt) 228.5
    11 Diesel A CH-7 (10% wt.) 214.5
    B* Diesel B 624
    12 Diesel B CH-5 (500 ppmw) 335
    13 Diesel B CH-5 (1000 ppmw) 365
    14 Diesel B CH-5 (1% wt) 281.5
    15 Diesel B CH-5 (10% wt.) 246.5
    16 Diesel B CH-7 (500 ppmw) 427.5
    17 Diesel B CH-7 (1000 ppmw) 386.5
    18 Diesel B CH-7 (1% wt) 304
    19 Diesel B CH-7 (10% wt.) 216
    C* Diesel C 624.5
    20 Diesel c CH-5 (100 ppmw) 442.5
    21 Diesel C CH-5 (1000 ppmw) 376.5
    22 Diesel c CH-5 (1% wt) 289.5
    23 Diesel C CH-5 (10% wt.) 228.5
    24 Diesel c CH-7 (500 ppmw) 471
    25 Diesel C CH-7 (1000 ppmw) 335
    26 Diesel c CH-7 (1% wt) 255.5
    27 Diesel C CH-7 (10% wt.) 209
    D* Gasoline 907
    28 Gasoline CH-5 (50 ppmw) 630.5
    29 Gasoline CH-5 (100 ppmw) 412.5
    30 Gasoline CH-5 (500 ppmw) 308.5
    31 Gasoline CH-5 (1000 ppmw) 346
    32 Gasoline CH-5 (1% wt) 229.5
    33 Gasoline CH-5 (10% wt.) 202.5
    34 Gasoline CH-7 (50 ppmw) 861.5
    35 Gasoline CH-7 (100 ppmw) 639
    36 Gasoline CH-7 (500 ppmw) 358
    37 Gasoline CH-7 (1000 ppmw) 347
    38 Gasoline CH-7 (1% wt) 206.5
    39 Gasoline CH-7 (10% wt.) 206.5
    *Not according to the present invention.
  • As can be seen from the results in Table 4, a reduced wear scar is observed in the HFRR test for the fuel compositions (both gasoline and diesel fuel compositions) containing the CH-5 and CH-7 hyperdispersants compared to the base fuel, which represents an improvement in lubricity of the fuels containing the hyperdispersant compared to the base fuel.
  • Example 40
  • Inlet valve deposit (IVD) keep clean tests were performed for two gasoline compositions prepared by blending a base gasoline as described in Table 5 below with 400 ppmw and 1000 ppmw of the CH-5 hyperdispersant.
  • TABLE 5
    Gasoline base fuel.
    Parameter
    RON (ASTM D2699) 98.9
    MON (ASTM D2700) 87.3
    Density at 15° C. (IP365) 0.7758 g/cm3
    IBP (IP123) 33.3° C.
    10% rec. (IP123) 56.4° C.
    20% rec. (IP123) 78.2° C.
    30% rec. (IP123) 96.8° C.
    40% rec. (IP123) 109.3° C.
    50% rec. (IP123) 118.6° C.
    60% rec. (IP123) 127.0° C.
    70% rec. (IP123) 136.4° C.
    80% rec. (IP123) 147.5° C.
    90% rec. (IP123) 161.4° C.
    95% rec. (IP123) 171.8° C.
    FBP (IP123) 202.9° C.
    RVP (IP394) 62.2 kPa
    Olefins (inc. dienes) 7.44% vol.
    Aromatics 49.78% vol.
  • The IVD test was performed in a Toyota 2.0 L 3S-FE bench engine using the CEC-F-05-A-93 M102E operating cycle modified by BMEP to the torque conditions detailed in Table 6 below. The Toyota engine has been modified to concurrently run two fuel systems, one fuelling cylinders 1 and 2 and a second fuelling cylinders 3 and 4. The engine starts with clean valves and combustion chamber and is run for 69 hr on the test fuels. At the end of the 69 hours the engine is stripped, the valves weighed to determine the level of deposits.
  • TABLE 6
    Engine test cycle details for Toyota DF engine
    Coolant Oil out
    Stage Stage Engine Torque out temp temp
    No time (s) speed (rpm) (Nm) (° C.) (° C.)
    1 30 800 0 90 97
    2 60 1300 26 90 97
    3 120 1850 28 90 97
    4 60 3000 30 90 97
  • The gasoline containing 400 and 1000 ppmw respectively of CH-5 was tested in the Toyota 3S-FE dual fuelled engine with the 400 ppmw CH-5 gasoline test blend in cylinders 1 and 2 and the 1000 ppmw CH-5 gasoline test blend in cylinders 3 and 4.
  • The average weight of the inlet valve deposits for cylinders 1 and 2 was 194.6 mg and for cylinders 3 and 4 was 130.0 mg. An average level of deposit observed with a gasoline containing no additives in a 69 hour test is typically about 200 mg.
  • Example 41
  • The injector nozzle keep clean performance of the CH-5 hyperdispersant in diesel fuel was assessed using the CEC SG-F-098 test procedure. The diesel fuel used in the test procedure contained 300 ppmw of the CH-5 hyperdispersant. In the test, up until 24 hours no power loss was observed and at 32 hours a power loss equating to 3% was observed. At this point the equivalent power loss for the reference fuel was 9%.
  • Preparation of Non-Sulfur-Containing Poly(Hydroxycarboxylic Acid) Amide Salt Derivatives Example E
  • 8 gram of the poly(hydroxycarboxylic acid) amide salt derivative commercially available from Shanghai Sanzheng Polymer Company under the trade designation “CH-5” was dissolved in 140 ml of dichloromethane (DCM) whilst stirring. The resultant mixture was further diluted with 110 ml DCM and added to a separation funnel containing 250 ml of 1M KOH solution.
  • The funnel was shaken and allowed to stand until there was clear separation between the two layers. The organic bottom layer was collected and added to 250 ml of fresh 1M KOH in a separation funnel. Again, the organic bottom layer was collected, dried over MgSO4 and concentrated in vacuo. About 6 gram of poly(hydroxycarboxylic acid) amide salt derivative wherein the anion Xq− is OH was obtained.
  • The obtained poly(hydroxycarboxylic acid) amide salt derivative had a TBN content of 7.4 mg·KOH/g (according to ASTM D 4739).
  • Example F
  • The “CH-5” product (see Example E) was ion-exchanged with a sodium salicylate (available from Sigma-Aldrich Chemical Company, Gillingham, United Kingdom) in a ion-exchange column, whilst using 1:3 MeOH:CHCl3 as an eluent.
  • To this end, a column was prepared using 500 gram Dowex 1×8 ion-exchange resin (200-400 mesh, strongly basic Cl form; CAS nr [69011-19-4]) which was washed in 1 l of deionised water. The washed Dowex resin was then loaded as a suspension onto a column using 1 l of 1:1 MeOH:de-ionised water. The resin was then washed with 4 bed volumes of 1:1 methanol/de-ionised water and loaded with a 30 wt. % solution of the sodium salicylate salt of in a small amount of MeOH.
  • Subsequent polarity change of the resin was done in the following order: 2×4 bed volumes of 1:1 MeOH/de-ionised water; 1×4 bed volumes of MeOH; 4 bed volumes of 3:1, then 1:1, then 1:3 of MeOH:chloroform.
  • 220 gram of the “CH-5” product was dissolved in a minimum amount of eluent (1:3 MeOH:chloroform) and loaded onto the column. The column was eluted, whilst following the elution by means of thin layer chromatography using appropriate staining techniques. The eluent was collected and concentrated in vacuo to dryness to yield about 200 gram of poly(hydroxycarboxylic acid) amide salt derivative wherein the anion Xq− is salicylate.
  • The obtained poly(hydroxycarboxylic acid) amide salt derivative had a TBN content of 8.2 mg·KOH/g (according to ASTM D 4739).
  • Example G
  • Similar to Example F, a poly(hydroxycarboxylic acid) amide salt derivative was obtained wherein the anion Xq− is a phenate. To this end sodium phenoate (available from Sigma-Aldrich Chemical Company, Gillingham, United Kingdom) was used.
  • The obtained poly(hydroxycarboxylic acid) amide salt derivative had a TBN content of 8.5 mg·KOH/g (according to ASTM D 4739).
  • Example H
  • Similar to Example F, a poly(hydroxycarboxylic acid) amide salt derivative was obtained wherein the anion Xq− is an oleate. To this end sodium oleate (available from Sigma-Aldrich Chemical Company, Gillingham, United Kingdom) was used.
  • The obtained poly(hydroxycarboxylic acid) amide salt derivative had a TBN content of 7.9 mg·KOH/g (according to ASTM D 4739).
  • Example I
  • Similar to Example F, a poly(hydroxycarboxylic acid) amide salt derivative was obtained wherein the anion Xq− is an acetate. To this end sodium acetate (available from Sigma-Aldrich Chemical Company, Gillingham, United Kingdom) was used.
  • The obtained poly(hydroxycarboxylic acid) amide salt derivative had a TBN content of 8.5 mg·KOH/g (according to ASTM D 4739).
  • Engine Lubricant Performance
  • The performance of the crankcase lubricant of an engine fuelled using a liquid fuel composition according to the present invention was assessed using the Sequence VG test, ASTM D 6593-07.
  • Two separate poly(hydroxycarboxylic acid) amide salt derivatives were assessed using in the Sequence VG tests. The base fuel used for both poly(hydroxycarboxylic acid) amide salt derivatives was an ASTM VG base fuel.
  • Fuel “Base” is ASTM VG base fuel.
  • Fuel “F-A” is “Base”+500 ppmw of “CH-5”.
  • Fuel “F-B” is “Base”+200 ppmw of Example F.
  • Lubricant “L-A” is an SF grade lubricant.
  • Lubricant “L-B” is a SL/CF grade lubricant.
  • The results of the Sequence VG tests are provided in Table 7 below. The “merit” rating used in the results is on a scale of 0 to 10, with 10 representing the rating of the condition of the component when new, and a single number increase in the “merit” rating represents a reduction in the sludge or varnish by half.
  • TABLE 7
    Sequence VG test results
    Final Original Unit Results
    Average Rocker Average Average
    Engine Cover Engine Piston
    Sludge Sludge Varnish Skirt
    Example Fuel Lubricant (merits) (merits) (merits) Varnish
    42 F-A L-A 9.71 9.79 9.82 9.69
    J* Base L-A 7.88 9.42 8.99 7.60
    43 F-B L-B 9.78 9.74 9.92 9.99
    K* Base L-B 9.28 9.41 9.28 8.26
    44 F-B L-B 9.80 9.73 9.98 10.00
    *Comparative TS 7750
  • As can clearly be seen from the results given in Table 7 above, the use of poly(hydroxycarboxylic acid) amide salt derivatives in the gasoline compositions results in a significant improvement in the performance of the lubricant in terms of inhibition of sludge and varnish deposit formation.

Claims (20)

1. A liquid fuel composition comprising:
a) a base fuel suitable for use in an internal combustion engine; and
b) one or more poly(hydroxycarboxylic acid) amide salt derivatives having formula (III):

[Y—CO[O-A-CO]n-Zr-R+]mpXq−  (III)
wherein Y is hydrogen or an optionally substituted hydrocarbyl group, A is a divalent optionally substituted hydrocarbyl group, n is from 1 to 100, m is from 1 to 4, q is from 1 to 4 and p is an integer such that pq=m, Z is an optionally substituted divalent bridging group which is attached to the carbonyl group through a nitrogen atom, r is 0 or 1, R+ is an ammonium group and Xq− is an anion.
2. The liquid fuel composition of claim 1 wherein the amount of the one or more poly(hydroxycarboxylic acid) amide salt derivatives present in the liquid fuel composition is at least 1 ppmw, based on the overall weight of the liquid fuel composition.
3. The liquid fuel composition of claim 2 wherein the amount of the one or more poly(hydroxycarboxylic acid) amide salt derivatives present in the liquid fuel composition is in the range of from 10 ppmw to 20% wt, based on the overall weight of the liquid fuel composition.
4. The liquid fuel composition of claim 1 wherein the anion, Xq−, is a non-sulphur-containing anion, preferably the anion, Xq−, is selected from anions derived from compounds containing a carboxylic acid group, anions derived from compounds containing a hydroxyl group, nitrogen based anions, phosphorus based anions, and mixtures thereof.
5. The liquid fuel composition of claim 4 wherein the amount of the one or more poly(hydroxycarboxylic acid) amide salt derivatives present in the liquid fuel composition is at least 1 ppmw, based on the overall weight of the liquid fuel composition.
6. The liquid fuel composition of claim 5 wherein the amount of the one or more poly(hydroxycarboxylic acid) amide salt derivatives present in the liquid fuel composition is in the range of from 10 ppmw to 20% wt, based on the overall weight of the liquid fuel composition.
7. The liquid fuel composition of claim 1 wherein the anion, Xq−, is a sulphur-based anion, preferably the anion, Xq−, is selected from sulphate, sulphonate and mixtures thereof.
8. The liquid fuel composition of claim 7 wherein the amount of the one or more poly(hydroxycarboxylic acid) amide salt derivatives present in the liquid fuel composition is at least 1 ppmw, based on the overall weight of the liquid fuel composition.
9. The liquid fuel composition of claim 8 wherein the amount of the one or more poly(hydroxycarboxylic acid) amide salt derivatives present in the liquid fuel composition is in the range of from 10 ppmw to 20% wt, based on the overall weight of the liquid fuel composition.
10. The liquid fuel composition of claim 7 wherein the one or more of the poly(hydroxycarboxylic acid) amide salt derivatives have a sulphur content in the range of from 0.1 to 2.0 wt. %, based on the total weight of said poly(hydroxycarboxylic acid) amide salt derivatives.
11. The liquid fuel composition of claim 1 wherein the one or more of the poly(hydroxycarboxylic acid) amide salt derivatives have a TBN (total base number) value of less than 10 mg·KOH/g.
12. The liquid fuel composition of claim 3 wherein the one or more of the poly(hydroxycarboxylic acid) amide salt derivatives have a TBN (total base number) value of less than 10 mg·KOH/g.
13. The liquid fuel composition of claim 4 wherein the one or more of the poly(hydroxycarboxylic acid) amide salt derivatives have a TBN (total base number) value of less than 10 mg·KOH/g.
14. The liquid fuel composition of claim 7 wherein the one or more of the poly(hydroxycarboxylic acid) amide salt derivatives have a TBN (total base number) value of less than 10 mg·KOH/g.
15. The liquid fuel composition of claim 1 wherein the base fuel is a gasoline.
16. The liquid fuel composition of claim 1 wherein the base fuel is a diesel fuel.
17. A method of operating an internal combustion engine, which method comprises introducing into a combustion chamber of the engine a liquid fuel composition of claims 1.
18. A method of operating an internal combustion engine, which method comprises introducing into a combustion chamber of the engine a liquid fuel composition of claims 3.
19. A method of operating an internal combustion engine, which method comprises introducing into a combustion chamber of the engine a liquid fuel composition of claims 4.
20. A method of operating an internal combustion engine, which method comprises introducing into a combustion chamber of the engine a liquid fuel composition of claims 7.
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Publication number Priority date Publication date Assignee Title
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Publication number Priority date Publication date Assignee Title
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EP3334805B1 (en) * 2015-08-13 2019-05-15 Shell International Research Maatschappij B.V. Process for fuel formulation

Citations (29)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3275554A (en) * 1963-08-02 1966-09-27 Shell Oil Co Polyolefin substituted polyamines and lubricants containing them
US3438757A (en) * 1965-08-23 1969-04-15 Chevron Res Hydrocarbyl amines for fuel detergents
US3454555A (en) * 1965-01-28 1969-07-08 Shell Oil Co Oil-soluble halogen-containing polyamines and polyethyleneimines
US3755433A (en) * 1971-12-16 1973-08-28 Texaco Inc Ashless lubricating oil dispersant
US3822209A (en) * 1966-02-01 1974-07-02 Ethyl Corp Lubricant additives
US3996059A (en) * 1971-12-30 1976-12-07 Imperial Chemical Industries Limited Dispersing agents
US4208190A (en) * 1979-02-09 1980-06-17 Ethyl Corporation Diesel fuels having anti-wear properties
US4349389A (en) * 1979-07-26 1982-09-14 Imperial Chemical Industries Limited Dispersible inorganic pigment
US4512903A (en) * 1983-06-23 1985-04-23 Texaco Inc. Lubricant compositions containing amides of hydroxy-substituted aliphatic acids and fatty amines
US4512776A (en) * 1983-12-23 1985-04-23 Exxon Research And Engineering Co. Ionic polymer-polylactone compositions as flow improvers for oils and fuels
US4525288A (en) * 1983-08-15 1985-06-25 Texaco Inc. Lubricants containing hydroxyalkoxy acid amides of alkyl amines as friction reducers
US4746739A (en) * 1984-11-23 1988-05-24 International Paint Public Limited Company Dispersants
US4814010A (en) * 1987-01-27 1989-03-21 Imperial Chemical Industries Plc Corrosion inhibition
US5000792A (en) * 1988-06-09 1991-03-19 501 Sakata Inkusu Kabushikikaisha Pigment dispersing agent and offset printing ink composition employing the same
US5139692A (en) * 1991-05-20 1992-08-18 General Motors Corporation Electrorheological compositions including an amine-terminated polyester steric stabilizer
US5149454A (en) * 1991-05-20 1992-09-22 General Motors Corporation Electrorheological compositions including am5-11 O8-17
US5378348A (en) * 1993-07-22 1995-01-03 Exxon Research And Engineering Company Distillate fuel production from Fischer-Tropsch wax
US5490864A (en) * 1991-08-02 1996-02-13 Texaco Inc. Anti-wear lubricity additive for low-sulfur content diesel fuels
US5536445A (en) * 1984-03-21 1996-07-16 Zeneca Limted Surfactant and dispersible or emulsifiable compositions employing surfactant
US5766274A (en) * 1997-02-07 1998-06-16 Exxon Research And Engineering Company Synthetic jet fuel and process for its production
US5855629A (en) * 1996-04-26 1999-01-05 Shell Oil Company Alkoxy acetic acid derivatives
US5858029A (en) * 1997-01-13 1999-01-12 Mobil Oil Corporation Friction reducing additives for fuels and lubricants
US5888376A (en) * 1996-08-23 1999-03-30 Exxon Research And Engineering Co. Conversion of fischer-tropsch light oil to jet fuel by countercurrent processing
US5952274A (en) * 1996-08-27 1999-09-14 Schill & Seilacher Gmbh & Co. Use of polyhydroxycarboxylamides as EP additives
US6204426B1 (en) * 1999-12-29 2001-03-20 Chevron U.S.A. Inc. Process for producing a highly paraffinic diesel fuel having a high iso-paraffin to normal paraffin mole ratio
US20020065201A1 (en) * 2000-09-21 2002-05-30 Marc Ribeaud Lubricants with 5-tert.-butyl-4-hydroxy-3-methylphenyl substituted fatty acid esters
US6458173B1 (en) * 1998-12-04 2002-10-01 Infineum International Ltd. Fuel additive and fuel composition containing the same
US6599864B1 (en) * 1999-09-08 2003-07-29 Total Raffinage Distribution S.A. Hydrocarbon base oil for lubricants with very high viscosity index
US20080026973A1 (en) * 2006-05-03 2008-01-31 Nelson David C Lubricating oil composition

Family Cites Families (44)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3306908A (en) * 1963-12-26 1967-02-28 Lubrizol Corp Reaction products of high molecular weight hydrocarbon succinic compounds, amines and heavy metal compounds
GB1342746A (en) 1970-12-22 1974-01-03
BE793279A (en) * 1971-12-30 1973-06-22 Ici Ltd DISPERSING AGENTS
NL184322C (en) 1976-10-18 1989-06-16 Shell Int Research PROCESS FOR PREPARING AN OIL-SOLUBLE POLYMER AND LUBRICATING OIL COMPOSITION CONTAINING IT.
GB1543359A (en) 1976-10-28 1979-04-04 Shell Int Research Esterification of hydrocarbyl-substituted succinic anhydrides
GB2001083B (en) 1977-07-15 1982-06-30 Ici Ltd Dispersing agents dispersions containing these agents and paints and links made from the dispersions
GB2061958B (en) 1979-10-24 1983-07-20 Shell Int Research Process for the preparation of polyalkenyl-substituted succinic anhydride
GB2115000B (en) 1982-02-17 1985-02-06 Shell Int Research Lubricating oils and hydraulic fluids
US4715973A (en) 1985-03-15 1987-12-29 Shell Oil Company Lubricating oil compositions
US4866142A (en) * 1986-10-07 1989-09-12 Exxon Chemical Patents Inc. Lactone modified polymeric amines useful as oil soluble dispersant additives
GB9008811D0 (en) * 1990-04-19 1990-06-13 Exxon Chemical Patents Inc Chemical compositions and their use as fuel additives
GB9326374D0 (en) 1993-12-23 1994-02-23 Zeneca Ltd Process
EP0668342B1 (en) 1994-02-08 1999-08-04 Shell Internationale Researchmaatschappij B.V. Lubricating base oil preparation process
US5646212A (en) 1994-09-02 1997-07-08 Ici Americas Inc. Polyalkylene glycol anhydroxy carboxylic acid dispersant
EP0776959B1 (en) 1995-11-28 2004-10-06 Shell Internationale Researchmaatschappij B.V. Process for producing lubricating base oils
CA2237068C (en) 1995-12-08 2005-07-26 Exxon Research And Engineering Company Biodegradable high performance hydrocarbon base oils
GB9610363D0 (en) * 1996-05-17 1996-07-24 Ethyl Petroleum Additives Ltd Fuel additives and compositions
US6090989A (en) 1997-10-20 2000-07-18 Mobil Oil Corporation Isoparaffinic lube basestock compositions
US6059955A (en) 1998-02-13 2000-05-09 Exxon Research And Engineering Co. Low viscosity lube basestock
US6008164A (en) 1998-08-04 1999-12-28 Exxon Research And Engineering Company Lubricant base oil having improved oxidative stability
US6165949A (en) 1998-09-04 2000-12-26 Exxon Research And Engineering Company Premium wear resistant lubricant
US6475960B1 (en) 1998-09-04 2002-11-05 Exxonmobil Research And Engineering Co. Premium synthetic lubricants
US6080301A (en) 1998-09-04 2000-06-27 Exxonmobil Research And Engineering Company Premium synthetic lubricant base stock having at least 95% non-cyclic isoparaffins
US6103099A (en) 1998-09-04 2000-08-15 Exxon Research And Engineering Company Production of synthetic lubricant and lubricant base stock without dewaxing
US6332974B1 (en) 1998-09-11 2001-12-25 Exxon Research And Engineering Co. Wide-cut synthetic isoparaffinic lubricating oils
US6361573B1 (en) * 1999-08-31 2002-03-26 Ethyl Corporation Fuel dispersants with enhanced lubricity
US7067049B1 (en) 2000-02-04 2006-06-27 Exxonmobil Oil Corporation Formulated lubricant oils containing high-performance base oils derived from highly paraffinic hydrocarbons
JP4330260B2 (en) 2000-08-31 2009-09-16 サカタインクス株式会社 Oil-based inkjet recording ink
US6610637B2 (en) * 2001-02-13 2003-08-26 The Lubrizol Corporation Synthetic diesel engine lubricants containing dispersant-viscosity modifier and functionalized phenol detergent
US6784143B2 (en) 2001-05-11 2004-08-31 Infineum International Ltd. Lubricating oil composition
FR2827608B1 (en) * 2001-07-17 2004-01-16 Elf Antar France POLYMERS BASED ON OLEFIN AND ALKENYL ALKYLATE AND THEIR USE AS MULTIFUNCTIONAL ADDITIVE IN FUELS AND FUELS
EP1513915B1 (en) 2002-06-10 2008-08-13 The Lubrizol Corporation Method of lubricating an internal combustion engine and improving the efficiency of the emissions control system of the engine
DE102004005179B4 (en) 2004-02-02 2006-07-13 Wobben, Aloys, Dipl.-Ing. Wind turbine
EP1824950A1 (en) * 2004-10-25 2007-08-29 The Lubrizol Corporation Corrosion inhibition
WO2006047745A1 (en) * 2004-10-27 2006-05-04 The Lubrizol Corporation Asphaltene inhibition
GB0425509D0 (en) 2004-11-19 2004-12-22 Ici Plc Dispersant
EP1728848B1 (en) 2005-06-01 2013-08-07 Infineum International Limited Use of unsaturated olefin polymers to improve the compatibility between nitrile rubber seals and lubricating oil compositions
EP3406692A1 (en) * 2005-06-16 2018-11-28 The Lubrizol Corporation Fuel composition comprising a quaternary ammonium salt detergent
EP1757673B1 (en) 2005-08-23 2020-04-15 Chevron Oronite Company LLC Lubricating oil composition for internal combustion engines
CN101484415B (en) * 2006-07-09 2013-08-14 于崇曦 Positively charged water-soluble prodrugs of aspirin
WO2009050287A1 (en) 2007-10-19 2009-04-23 Shell Internationale Research Maatschappij B.V. Functional fluids for internal combustion engines
EP2055729A1 (en) * 2007-10-23 2009-05-06 Shell Internationale Researchmaatschappij B.V. Lubricating composition
CN102124086A (en) * 2008-07-31 2011-07-13 国际壳牌研究有限公司 Poly(hydroxycarboxylic acid) amide salt derivative and lubricating composition containing it
US8414010B2 (en) * 2010-11-19 2013-04-09 Cnh America Llc System and method for drawbar support

Patent Citations (31)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3275554A (en) * 1963-08-02 1966-09-27 Shell Oil Co Polyolefin substituted polyamines and lubricants containing them
US3454555A (en) * 1965-01-28 1969-07-08 Shell Oil Co Oil-soluble halogen-containing polyamines and polyethyleneimines
US3438757A (en) * 1965-08-23 1969-04-15 Chevron Res Hydrocarbyl amines for fuel detergents
US3565804A (en) * 1965-08-23 1971-02-23 Chevron Res Lubricating oil additives
US3822209A (en) * 1966-02-01 1974-07-02 Ethyl Corp Lubricant additives
US3755433A (en) * 1971-12-16 1973-08-28 Texaco Inc Ashless lubricating oil dispersant
US3996059A (en) * 1971-12-30 1976-12-07 Imperial Chemical Industries Limited Dispersing agents
US4208190A (en) * 1979-02-09 1980-06-17 Ethyl Corporation Diesel fuels having anti-wear properties
US4349389A (en) * 1979-07-26 1982-09-14 Imperial Chemical Industries Limited Dispersible inorganic pigment
US4512903A (en) * 1983-06-23 1985-04-23 Texaco Inc. Lubricant compositions containing amides of hydroxy-substituted aliphatic acids and fatty amines
US4525288A (en) * 1983-08-15 1985-06-25 Texaco Inc. Lubricants containing hydroxyalkoxy acid amides of alkyl amines as friction reducers
US4512776A (en) * 1983-12-23 1985-04-23 Exxon Research And Engineering Co. Ionic polymer-polylactone compositions as flow improvers for oils and fuels
US5536445A (en) * 1984-03-21 1996-07-16 Zeneca Limted Surfactant and dispersible or emulsifiable compositions employing surfactant
US4746739A (en) * 1984-11-23 1988-05-24 International Paint Public Limited Company Dispersants
US4814010A (en) * 1987-01-27 1989-03-21 Imperial Chemical Industries Plc Corrosion inhibition
US5000792A (en) * 1988-06-09 1991-03-19 501 Sakata Inkusu Kabushikikaisha Pigment dispersing agent and offset printing ink composition employing the same
US5149454A (en) * 1991-05-20 1992-09-22 General Motors Corporation Electrorheological compositions including am5-11 O8-17
US5279753A (en) * 1991-05-20 1994-01-18 General Motors Corporation Water free electrorheological compositions including AM5-11 O8-17 where M is Al
US5139692A (en) * 1991-05-20 1992-08-18 General Motors Corporation Electrorheological compositions including an amine-terminated polyester steric stabilizer
US5490864A (en) * 1991-08-02 1996-02-13 Texaco Inc. Anti-wear lubricity additive for low-sulfur content diesel fuels
US5378348A (en) * 1993-07-22 1995-01-03 Exxon Research And Engineering Company Distillate fuel production from Fischer-Tropsch wax
US5855629A (en) * 1996-04-26 1999-01-05 Shell Oil Company Alkoxy acetic acid derivatives
US5888376A (en) * 1996-08-23 1999-03-30 Exxon Research And Engineering Co. Conversion of fischer-tropsch light oil to jet fuel by countercurrent processing
US5952274A (en) * 1996-08-27 1999-09-14 Schill & Seilacher Gmbh & Co. Use of polyhydroxycarboxylamides as EP additives
US5858029A (en) * 1997-01-13 1999-01-12 Mobil Oil Corporation Friction reducing additives for fuels and lubricants
US5766274A (en) * 1997-02-07 1998-06-16 Exxon Research And Engineering Company Synthetic jet fuel and process for its production
US6458173B1 (en) * 1998-12-04 2002-10-01 Infineum International Ltd. Fuel additive and fuel composition containing the same
US6599864B1 (en) * 1999-09-08 2003-07-29 Total Raffinage Distribution S.A. Hydrocarbon base oil for lubricants with very high viscosity index
US6204426B1 (en) * 1999-12-29 2001-03-20 Chevron U.S.A. Inc. Process for producing a highly paraffinic diesel fuel having a high iso-paraffin to normal paraffin mole ratio
US20020065201A1 (en) * 2000-09-21 2002-05-30 Marc Ribeaud Lubricants with 5-tert.-butyl-4-hydroxy-3-methylphenyl substituted fatty acid esters
US20080026973A1 (en) * 2006-05-03 2008-01-31 Nelson David C Lubricating oil composition

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9239000B2 (en) * 2010-05-25 2016-01-19 The Lubrizol Corporation Method to provide power gain in an engine
EP3705555A1 (en) * 2010-05-25 2020-09-09 The Lubrizol Corporation Method to provide power gain in an engine
EP2576738B1 (en) 2010-05-25 2020-04-08 The Lubrizol Corporation Use of a quaternary ammonium salt to provide a gain in power in a diesel engine
CN102906235A (en) * 2010-05-25 2013-01-30 卢布里佐尔公司 Method to provide power gain in engine
US20130233267A1 (en) * 2010-05-25 2013-09-12 The Lubrizol Corporation Method to Provide Power Gain in an Engine
WO2011149799A1 (en) * 2010-05-25 2011-12-01 The Lubrizol Corporation Method to provide power gain in an engine
EP2643384A1 (en) * 2010-11-24 2013-10-02 The Lubrizol Corporation Polyester quaternary ammonium salts
US20140338624A1 (en) * 2011-05-30 2014-11-20 Shell Oil Company Liquid fuel compositions
US9249699B2 (en) 2011-06-21 2016-02-02 The Lubrizol Corporation Lubricating composition containing a dispersant
WO2012177537A1 (en) 2011-06-21 2012-12-27 The Lubrizol Corporation Lubricating composition containing a dispersant
WO2012177549A1 (en) 2011-06-21 2012-12-27 The Lubrizol Corporation Lubricating composition containing a dispersant
US20140364661A1 (en) * 2011-12-21 2014-12-11 Zhongxin Huo Method and composition for reducing viscosity of a hydrocarbon mixture
US20140345190A1 (en) * 2011-12-21 2014-11-27 Shell Oil Company Method and composition for inhibiting foam in a hydrocarbon mixture
US9453173B2 (en) * 2011-12-21 2016-09-27 Shell Oil Company Method and composition for inhibiting foam in a hydrocarbon mixture
US8863700B2 (en) 2012-06-13 2014-10-21 Afton Chemical Corporation Fuel additive for improved performance in fuel injected engines
US20160017246A1 (en) * 2013-03-01 2016-01-21 Tonengeneral Sekiyu K.K. Fuel oil
US9340742B1 (en) 2015-05-05 2016-05-17 Afton Chemical Corporation Fuel additive for improved injector performance

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