[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

EP0795596A1 - Fuel compositions - Google Patents

Fuel compositions Download PDF

Info

Publication number
EP0795596A1
EP0795596A1 EP97200775A EP97200775A EP0795596A1 EP 0795596 A1 EP0795596 A1 EP 0795596A1 EP 97200775 A EP97200775 A EP 97200775A EP 97200775 A EP97200775 A EP 97200775A EP 0795596 A1 EP0795596 A1 EP 0795596A1
Authority
EP
European Patent Office
Prior art keywords
fuel
fuel composition
composition according
range
furan derivative
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP97200775A
Other languages
German (de)
French (fr)
Other versions
EP0795596B1 (en
Inventor
David John Barratt
Gautam Tavanappa Kalghatgi
Jian Lin
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shell Internationale Research Maatschappij BV
Original Assignee
Shell Internationale Research Maatschappij BV
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shell Internationale Research Maatschappij BV filed Critical Shell Internationale Research Maatschappij BV
Priority to EP97200775A priority Critical patent/EP0795596B1/en
Publication of EP0795596A1 publication Critical patent/EP0795596A1/en
Application granted granted Critical
Publication of EP0795596B1 publication Critical patent/EP0795596B1/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/185Ethers; Acetals; Ketals; Aldehydes; Ketones
    • C10L1/1852Ethers; Acetals; Ketals; Orthoesters
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/143Organic compounds mixtures of organic macromolecular compounds with organic non-macromolecular compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/185Ethers; Acetals; Ketals; Aldehydes; Ketones
    • C10L1/1852Ethers; Acetals; Ketals; Orthoesters
    • C10L1/1855Cyclic ethers, e.g. epoxides, lactides, lactones
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/185Ethers; Acetals; Ketals; Aldehydes; Ketones
    • C10L1/1857Aldehydes; Ketones
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/19Esters ester radical containing compounds; ester ethers; carbonic acid esters
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/198Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/222Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
    • C10L1/224Amides; Imides carboxylic acid amides, imides
    • 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
    • C10L1/232Organic compounds containing nitrogen containing nitrogen in a heterocyclic ring
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/04Use of additives to fuels or fires for particular purposes for minimising corrosion or incrustation
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/16Hydrocarbons
    • C10L1/1608Well defined compounds, e.g. hexane, benzene
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/16Hydrocarbons
    • C10L1/1616Hydrocarbons fractions, e.g. lubricants, solvents, naphta, bitumen, tars, terpentine
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/16Hydrocarbons
    • C10L1/1625Hydrocarbons macromolecular compounds
    • C10L1/1633Hydrocarbons macromolecular compounds homo- or copolymers obtained by reactions only involving carbon-to carbon unsaturated bonds
    • C10L1/1641Hydrocarbons macromolecular compounds homo- or copolymers obtained by reactions only involving carbon-to carbon unsaturated bonds from compounds containing aliphatic monomers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/182Organic compounds containing oxygen containing hydroxy groups; Salts thereof
    • C10L1/1822Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
    • C10L1/1824Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/182Organic 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
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/188Carboxylic acids; metal salts thereof
    • C10L1/1881Carboxylic acids; metal salts thereof carboxylic group attached to an aliphatic carbon atom
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/188Carboxylic acids; metal salts thereof
    • C10L1/1881Carboxylic acids; metal salts thereof carboxylic group attached to an aliphatic carbon atom
    • C10L1/1883Carboxylic acids; metal salts thereof carboxylic group attached to an aliphatic carbon atom polycarboxylic acid
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/19Esters ester radical containing compounds; ester ethers; carbonic acid esters
    • C10L1/1905Esters ester radical containing compounds; ester ethers; carbonic acid esters of di- or polycarboxylic acids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/19Esters ester radical containing compounds; ester ethers; carbonic acid esters
    • C10L1/191Esters ester radical containing compounds; ester ethers; carbonic acid esters of di- or polyhydroxyalcohols
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/198Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
    • C10L1/1985Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid polyethers, e.g. di- polygylcols and derivatives; ethers - esters
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/20Organic compounds containing halogen
    • C10L1/202Organic compounds containing halogen aromatic bond
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/222Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
    • C10L1/2222(cyclo)aliphatic amines; polyamines (no macromolecular substituent 30C); quaternair ammonium compounds; carbamates
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/222Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
    • C10L1/2222(cyclo)aliphatic amines; polyamines (no macromolecular substituent 30C); quaternair ammonium compounds; carbamates
    • C10L1/2225(cyclo)aliphatic amines; polyamines (no macromolecular substituent 30C); quaternair ammonium compounds; carbamates hydroxy containing
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/222Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
    • C10L1/223Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond having at least one amino group bound to an aromatic carbon atom
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/226Organic compounds containing nitrogen containing at least one nitrogen-to-nitrogen bond, e.g. azo compounds, azides, hydrazines
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/228Organic compounds containing nitrogen containing at least one carbon-to-nitrogen double bond, e.g. guanidines, hydrazones, semicarbazones, imines; containing at least one carbon-to-nitrogen triple bond, e.g. nitriles
    • C10L1/2286Organic compounds containing nitrogen containing at least one carbon-to-nitrogen double bond, e.g. guanidines, hydrazones, semicarbazones, imines; containing at least one carbon-to-nitrogen triple bond, e.g. nitriles containing one or more carbon to nitrogen triple bonds, e.g. nitriles
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/23Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites
    • C10L1/231Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites nitro compounds; nitrates; nitrites
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/238Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/238Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/2383Polyamines or polyimines, or derivatives thereof (poly)amines and imines; derivatives thereof (substituted by a macromolecular group containing 30C)
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • C10L1/234Macromolecular compounds
    • C10L1/238Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/2383Polyamines or polyimines, or derivatives thereof (poly)amines and imines; derivatives thereof (substituted by a macromolecular group containing 30C)
    • C10L1/2387Polyoxyalkyleneamines (poly)oxyalkylene amines and derivatives thereof (substituted by a macromolecular group containing 30C)
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2406Organic compounds containing sulfur, selenium and/or tellurium mercaptans; hydrocarbon sulfides
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2431Organic compounds containing sulfur, selenium and/or tellurium sulfur bond to oxygen, e.g. sulfones, sulfoxides
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2431Organic 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
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2443Organic compounds containing sulfur, selenium and/or tellurium heterocyclic compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic compounds containing sulfur, selenium and/or tellurium
    • C10L1/2443Organic compounds containing sulfur, selenium and/or tellurium heterocyclic compounds
    • C10L1/245Organic compounds containing sulfur, selenium and/or tellurium heterocyclic compounds only sulfur as hetero atom
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/24Organic 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
    • 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
    • C10L1/30Organic compounds compounds not mentioned before (complexes)
    • C10L1/305Organic compounds compounds not mentioned before (complexes) organo-metallic compounds (containing a metal to carbon bond)
    • 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
    • C10L1/30Organic compounds compounds not mentioned before (complexes)
    • C10L1/305Organic compounds compounds not mentioned before (complexes) organo-metallic compounds (containing a metal to carbon bond)
    • C10L1/306Organic compounds compounds not mentioned before (complexes) organo-metallic compounds (containing a metal to carbon bond) organo Pb compounds

Definitions

  • This invention relates to fuel compositions containing furan derivatives, a method of operating an internal combustion engine using such fuel compositions and to fuel additive concentrates.
  • octane requirement i.e. fuel octane number required for knock-free operation
  • fuel octane number required for knock-free operation
  • This level appears to correspond to a point in time when the quantity of deposit accumulation on the combustion chamber and valve surfaces no longer increases but remains relatively constant.
  • equilibrium value is normally reached between 3,000 and 20,000 miles (4,000 and 32,000 km) or corresponding hours of operation.
  • octane requirement increase control (ORIC) agents Fuel additives which inhibit or prevent deposit formation in the combustion chamber may be termed octane requirement increase control (ORIC) agents; those which remove or modify formed deposits, leading to decrease in octane requirements, may be termed octane requirement reduction (ORR) agents.
  • ORIC octane requirement increase control
  • ORR octane requirement reduction
  • US Patent No. 4,339,245 discloses the use of certain furyl compounds including furfuryl alcohol, furfuryl amine, ethylfurfurylacrylate, furfuryl acetate, furfuryl propionate, furfuryl isobutyrate, methyl furoate, ethyl furoate and compounds having alkyl groups substituted on the furyl rings as antiknock additives in gasoline.
  • Addition of the furyl compounds described increased the RON (research octane number) of the gasoline.
  • the RON is an intrinsic property of a gasoline, and is independent of any ORIC or ORR effect which that gasoline might, or might not, manifest in use. No ORIC or ORR activity is either described or hinted at in US Patent No. 4,339,245.
  • EP-A-174 123 discloses a process for the preparation of alkylfurans, and acknowledges that alkylfurans may be included in gasoline compositions as octane improving additives. As above, this relates to the RON of the gasoline, and not to any ORIC or ORR effect.
  • a fuel composition which comprises a major amount of a fuel boiling in the gasoline boiling range and a minor amount of an additive comprising a furan derivative containing a furyl group bearing one or more substituents comprising one or more heterocyclic and/or one or more aryl groups.
  • the or each heterocyclic group may be any optionally substituted saturated or unsaturated ring system, e.g. a 5 to 7 membered ring system, containing at least one heteroatom selected from oxygen, nitrogen and sulphur, 5- and 6-membered rings being preferred, e.g. a furyl, piperidinyl, pyridinyl, pyrrolyl, triazinyl, imidazolinyl or thiophenyl(thienyl) group.
  • 5-membered ring systems containing oxygen and/or nitrogen, preferably a furan or pyrrole ring.
  • the aryl group(s) may be any optionally substituted aryl group, preferably an optionally-substituted phenyl group.
  • Preferred aryl groups are phenyl groups which are unsubstituted or substituted by an alkyl group.
  • heterocyclic and/or aryl groups comprise unsaturated 5-membered ring systems containing oxygen and/or nitrogen, or benzene ring systems.
  • substituent groups for both the heterocyclic and aryl groups include halogen atoms (e.g. chlorine atoms), nitro, hydroxyl, carboxyl, amino, cyano, alkyl, formyl, alkoxycarbonyl, alkanoyl, alkylthio, alkylsulphinyl, alkylsulphonyl, carbamoyl and alkylamido groups.
  • halogen atoms e.g. chlorine atoms
  • nitro, hydroxyl, carboxyl, amino, cyano, alkyl, formyl, alkoxycarbonyl, alkanoyl, alkylthio, alkylsulphinyl, alkylsulphonyl, carbamoyl and alkylamido groups e.g. chlorine atoms
  • nitro hydroxyl
  • carboxyl amino
  • cyano alkyl
  • formyl alkoxycarbonyl
  • alkanoyl alkylthio
  • each heterocyclic group and/or aryl group is connected to the furyl group directly or by means of a bridging optionally substituted hydrocarbyl (preferably alkylene), carbonyl, dicarbonyl, amido, alkyleneamido, alkyleneoxyalkyl or alkoxycarbonyl group.
  • a bridging optionally substituted hydrocarbyl preferably alkylene
  • carbonyl, dicarbonyl, amido, alkyleneamido, alkyleneoxyalkyl or alkoxycarbonyl group may also be connected to a heterocyclic or aryl group which is connected to the furyl group, directly or via such a bridging group.
  • connections between furyl groups and heterocyclic or aryl groups as defined above or between heterocyclic or aryl groups and additional heterocyclic or aryl group are either direct connections or are bridging groups selected from C 1-4 alkylene (preferably -CH 2 -), -CH 2 NHCO-, -NHCO-, -CO-CO-, -CH 2 -O-CO- and -CH 2 OCH 2 - groups.
  • the furyl group bears a single substituent which comprises one or more heterocyclic and/or one or more aryl groups.
  • the number of heterocyclic and/or aryl groups present in addition in the furyl group may advantageously range from 1 to 5, preferably from 1 to 4.
  • the molecular weight of the furan derivative is preferably in the range from 100 to 5000, more preferably in the range 100 to 500 and most preferably 145 to 500.
  • the molecular weight corresponds to the formula weight of the compound.
  • the molecular weight is number average molecular weight, as determined by gel permeation chromatography (GPC), using polystyrene calibration standards.
  • suitable furan derivatives to be used in accordance with the present invention include those having the following general formula: wherein R1, R2, R3 and R4 each independently represent hydrogen, a heterocyclic group or an aryl group connected to the furyl group directly or by means of a bridging group as defined hereinbefore provided that at least one of R 1 , R 2 , R 3 and R 4 is such a heterocyclic group or an aryl group.
  • R3 and R4 represent an optionally substituted saturated or unsaturated ring system containing at least one heteroatom selected from oxygen, nitrogen and sulphur, connected to the furyl group as defined above.
  • a particularly preferred furan derivative for use in fuel compositions of the present invention is a furfuryl alcohol resin or a derivative thereof.
  • a furfuryl alcohol resin is defined as a polymer product obtained by condensation of optionally substituted furfuryl alcohol monomers (e.g. 2-furanmethanol monomers), or a distillation product thereof containing at least two furan rings.
  • the furfuryl alcohol resin has a number average molecular weight in the range of 145 (i.e. from about 150) to 5000, more preferably in the range of from 145 (about 150) to 500, as measured by gel permeation chromatography (GPC) using polystyrene calibration standards.
  • the furfuryl alcohol resin or derivative thereof comprises in addition to the furyl group a number of further furyl groups which are connected to the neighbouring furyl groups by means of an optionally substituted hydrocarbyl (preferably alkylene), alkyleneoxyalkyl or alkoxycarbyl group, e.g. a -CH 2 - or -CH 2 -O-CH 2 - group.
  • an optionally substituted hydrocarbyl preferably alkylene
  • alkyleneoxyalkyl or alkoxycarbyl group e.g. a -CH 2 - or -CH 2 -O-CH 2 - group.
  • the furfuryl alcohol resin comprises the condensation product of non-substituted 2-furanmethanol monomers.
  • the additional furyl groups are connected to the neighbouring furyl groups by means of a methylene group, or in some cases a -CH 2 -O-CH 2 -group.
  • Suitable monomers include those having the following general formula: wherein R1, R2, R4 and R5 each independently represent hydrogen, a hydrocarbyl group, a nitrogen-containing, an oxygen-containing or a sulphur-containing hydrocarbyl group and R3 represents hydrogen.
  • the hydrocarbyl group may conveniently comprise an aryl, alkyl, alkenyl or cycloalkyl group.
  • the hydrocarbyl group contains 2 to 50 carbon atoms, preferably 2 to 20 carbon atoms and more preferably 2 to 10 carbon atoms.
  • Suitable furfuryl alcohol resins or derivatives thereof include those obtained by polycondensation of different types of monomers (II).
  • the furfuryl alcohol resins or derivatives thereof to be applied in accordance with the present invention include those having the following general formulae (III) or (IV): wherein R 1 , R 2 , R 3 , R 4 and R 5 have the meanings as defined hereinabove for formula II, R 6 represents hydrogen, OH, and R 7 and R 8 represent an optionally nitrogen-containing, oxygen-containing or sulphur-containing hydrocarbyl group, x is in the range from 0 to 60, preferably from 0 to 30 and more preferably from 0 to 10, y is 0 or 1, z is in the range from 0 to 60, preferably from 0 to 30 and more preferably from 0 to 10, each of (x + z) and Z' ranges from 1 to 60, preferably 1 to 30 and more preferably from 1 to 10, and p is in the range from 1 to 80, preferably ranging from 5 to 25.
  • R 1 , R 2 , R 3 , R 4 and R 5 have the meanings as defined hereinabove for
  • furfuryl alcohol resin or derivatives thereof will usually comprise a mixture of any of the polymer products III and IV described above, and of course any unreacted 2-furanmethanol or derivative thereof.
  • the furfuryl alcohol resins may contain unreacted hydroxy groups which may subsequently be derivatised, e.g. esterified, in known manner.
  • a preferred derivative is an alkylsuccinic acid ester of a furfuryl resin, which may be prepared by reaction of the furfuryl resin with an olefin-succinic anhydride, e.g. a C 15-19 internal olefin-succinic anhydride.
  • a particularly preferred fuel composition according to the present invention is one wherein the furan derivative is selected from the group consisting of N-furfuryl-2-furamide, 2-amino-1-(2-furanylmethyl)-4,5-difuryl-3-pyrrolecarbonitrile, N-phenyl furamide, 1-furfurylpyrrole, furil, furfuryl benzoate, furfuryl resins having number average molecular weights in the range 145 to 500 and alkylsuccinic acid esters of furfuryl resins having number average molecular weights in said range.
  • the furan derivative is selected from the group consisting of N-furfuryl-2-furamide, 2-amino-1-(2-furanylmethyl)-4,5-difuryl-3-pyrrolecarbonitrile, N-phenyl furamide, 1-furfurylpyrrole, furil, furfuryl benzoate, furfuryl resins having number average molecular weights in the range 145 to 500 and alkylsucc
  • the additive comprising the furan derivative is preferably present in the fuel composition in an octane requirement reducing amount.
  • the fuel is present in a major amount (i.e. more than 50%w), and the additive comprising the furan derivative is present in a minor amount, preferably from 0.005 to 10%w, more preferably from 0.01 to 5%w, and most preferably from 0.02 to 1%w, based on the weight of the fuel composition.
  • the invention further provides an additive concentrate suitable for addition to fuel for an internal combustion engine which comprises a fuel-compatible diluent and an additive comprising a furan derivative as defined above, preferably in an amount of from 5 to 75%w calculated on the diluent.
  • a method of operating an internal combustion engine which comprises introducing into the combustion chambers of said engine a fuel composition as defined above according to the invention.
  • the fuel boiling in the gasoline boiling range may consist substantially of hydrocarbons or it may contain blending components. Alternatively, e.g. in countries such as Brazil, the fuel may consist substantially of ethanol.
  • Suitable liquid hydrocarbon fuels of the gasoline boiling range are mixtures of hydrocarbon boiling in the temperature range from about 25°C to about 232°C, and comprise mixtures of saturated hydrocarbons, olefinic hydrocarbons and aromatic hydrocarbons.
  • Preferred are gasoline mixtures having a saturated hydrocarbon content ranging from about 40% to about 80% by volume, an olefinic hydrocarbon content from 0% to about 30% by volume and an aromatic hydrocarbon content from about 10% to about 60% by volume.
  • the base fuel is derived from straight run gasoline, polymer gasoline, natural gasoline, dimer and trimerized olefins, synthetically produced aromatic hydrocarbon mixtures, from thermally or catalytically reformed hydrocarbons, or from catalytically cracked or thermally cracked petroleum stocks, and mixtures of these.
  • the hydrocarbon composition and octane level of the base fuel are not critical.
  • the octane level, (R+M)/2 will generally be above about 85 (where R is Research Octane Number and M is Motor Oct
  • Any conventional base gasoline can be employed in the practice of the present invention.
  • hydrocarbons in the gasoline can be replaced by up to a substantial amount of conventional alcohols or ethers, conventionally known for use in fuels.
  • the base gasolines are desirably substantially free of water since water could impede a smooth combustion.
  • the gasolines to which the invention is applied may be leaded or unleaded, although are preferably substantially lead-free, and may contain minor amounts of one or more blending agents such as methanol, ethanol, tertiary butanol, ethyl tertiary butyl ether, methyl tertiary butyl ether, and the like, at from about 0.1% by volume to about 25% by volume of the base fuel, although larger amounts (e.g. up to 40%v) may be utilised.
  • one or more blending agents such as methanol, ethanol, tertiary butanol, ethyl tertiary butyl ether, methyl tertiary butyl ether, and the like, at from about 0.1% by volume to about 25% by volume of the base fuel, although larger amounts (e.g. up to 40%v) may be utilised.
  • the gasolines may further suitably contain a nonionic surfactant, such as an alkylphenol or an alkyl alkoxylate.
  • a nonionic surfactant such as an alkylphenol or an alkyl alkoxylate.
  • Suitable examples of such surfactants include C 4 -C 18 -alkylphenol and C 2 -C 6 -alkylethoxylate or C 2 -C 6 -alkylpropoxylate or mixtures thereof.
  • the amount of the surfactant is advantageously from 10 to 1000 ppmw.
  • the gasoline can also contain other conventional additives including antioxidants such as phenolics, e.g. 2,6-di-tert-butylphenol or phenylenediamines, e.g. N,N'-di-sec-butyl-p-phenylenediamine, dyes, metal deactivators, dehazers such as polyester-type ethoxylated alkylphenol-formaldehyde resins.
  • antioxidants such as phenolics, e.g. 2,6-di-tert-butylphenol or phenylenediamines, e.g. N,N'-di-sec-butyl-p-phenylenediamine, dyes, metal deactivators, dehazers such as polyester-type ethoxylated alkylphenol-formaldehyde resins.
  • Corrosion inhibitors such as that commercially sold by Rhein Chemie, Mannheim, Germany as “RC 4801", or a polyhydric alcohol ester of a succinic acid derivative having on at least one of its alpha-carbon atoms an unsubstituted or substituted aliphatic hydrocarbon group having from 20 to 500 carbon atoms, for example, pentaerythritol diester of polyisobutylene-substituted succinic acid, the polyisobutylene group having an average molecular weight of about 950, in an amount from about 1 ppmw to about 1000 ppmw, may also be present.
  • the fuels can also contain antiknock compounds such as methyl cyclopentadienylmanganese tricarbonyl, tetraethyl lead or other lead-containing compounds, and ortho-azodiphenol as well as co-antiknock compounds such as benzoyl acetone.
  • antiknock compounds such as methyl cyclopentadienylmanganese tricarbonyl, tetraethyl lead or other lead-containing compounds, and ortho-azodiphenol as well as co-antiknock compounds such as benzoyl acetone.
  • a preferred gasoline composition of the invention may additionally contain a minor amount of at least one additional additive compound selected from the group consisting of polyalkenyl amines, Mannich amines, polyalkenyl succinimide, poly(oxyalkylene)amines, poly(oxyalkylene)carbamates, and poly(alkenyl)-N-substituted carbamates.
  • An effective amount of the additive comprising the furan derivative is introduced into the combustion zone of the engine in a variety of ways to prevent build-up of deposits or to accomplish the modification of existing deposits that are related to octane requirement.
  • a preferred method is to add a minor amount of a furan derivative as defined above to the gasoline.
  • one or more furan derivatives as defined above are added directly to the gasoline or are blended with one or more carriers and/or one or more hydrocarbon-soluble alkali metal or alkaline earth metal salts and/or one or more additional detergents before being added to the gasoline.
  • furan derivative used will depend on the particular furan derivative used, the fuel, and the presence or absence of carriers, detergents and diluents.
  • the carrier when utilised, may conveniently have an average molecular weight from about 250 to about 5000.
  • Suitable carriers include hydrocarbon based materials such as polyisobutylenes (PIB's), polypropylenes (PP's) and polyalphaolefins (PAO's), all of which may be hydrogenated or unhydrogenated but are preferably hydrogenated; polyether based materials such as polybutylene oxides (poly BO's), polypropylene oxides (poly PO's), polyhexadecene oxides (poly HO's) and mixtures thereof (i.e.
  • the carrier is preferably selected from PIB's, poly BO's and poly PO's with poly PO's being the most preferred.
  • a particularly prepared carrier fluid comprises a combination of a polyalphaolefin having a viscosity at 100°C in the range 2 x 10 -6 to 2 x 10 -5 m 2 /s (2 to 20 centistokes) being a hydrogenated oligomer containing 18 to 80 carbon atoms derived from at least one alphaolefinic monomer containing from 8 to 16 carbon atoms, and a polyoxyalkylene compound selected from glycols, mono- and diethers thereof, having number average molecular weight (M n ) in the range 400 to 3000, the weight ratio polyalphaolefin: polyoxyalkylene compound being in the range 1:10 to 10:1.
  • the polyalphaolefins are primarily trimers, tetramers and pentamers, and synthesis of such materials is outlined in Campen et al. , "Growing use of synlubes", Hydrocarbon Processing, February 1982, pages 75 to 82.
  • the polyalphaolefin is preferably derived from an alphaolefinic monomer containing from 8 to 12 carbon atoms. Polyalphaolefins derived from decene-1 have been found to be very effective.
  • the polyalphaolefin preferably has viscosity at 100°C in the range of 6 x 10 -6 to 1 x 10 -5 m 2 /s (6 to 10 centistokes). Polyalphaolefin having a viscosity at 100°C of 8 x 10 -6 m 2 /s (8 centistokes) has been found to be very effective.
  • Preferred polyoxyalkylene compounds for use in combination with these polyalphaolefins are described in EP-A-588429 (Applicants reference T 5677).
  • the carrier concentration in the final fuel composition is up to about 1000 ppm weight. When a carrier is present, the preferred concentration is from about 50 ppm by weight to about 400 ppm by weight, based on the total weight of the fuel composition.
  • hydrocarbon-soluble alkali metal or alkaline earth metal salt when utilised, may be one of those described in WO 87/01126, and the compounds of formula I are particularly suitable for incorporation, as additional component, in fuel compositions as described in WO 87/01126.
  • Preferred hydrocarbon-soluble alkali metal or alkaline earth metal salts are, however, alkali metal or alkaline earth metal salts of a succinic acid derivative.
  • Such a salt of a succinic acid derivative when utilised, will have as a substituent on one of its alpha-carbon atoms an unsubstituted or substituted aliphatic hydrocarbon group having from 20 to 200 carbon atoms.
  • the succinic acid derivative will have as a substituent on one of its alpha-carbon atoms an unsubstituted or substituted hydrocarbon group having from 20 to 200 carbon atoms which is connected to the other alpha-carbon atom by means of a hydrocarbon moiety having from 1 to 6 carbon atoms, forming a ring structure.
  • Suitable such salts are described for example in EP-A-207560 and in EP-A-491439.
  • the salts of the succinic acid derivative can be monobasic or dibasic. Monobasic salts in which the remaining carboxylic acid group has been transformed into an amide or ester group may also be used. Suitable alkali metal salts of a partial ester of an alkyl polyether alcohol with a succinic acid derivative are described in EP-A-491439.
  • Suitable metal salts include lithium, sodium, potassium, rubidium, caesium and calcium salts. Particularly preferred salts are described in EP-A-207560.
  • the aliphatic hydrocarbon substituent(s) of the succinic acid derivative is suitably derived from a polyolefin, the monomers of which have 2 to 6 carbon atoms.
  • convenient substituents include polyethylene, polypropylene, polybutylenes, polypentenes, polyhexenes or mixed polymers.
  • Particularly preferred is an aliphatic hydrocarbon group which is derived from polyisobutylene.
  • the hydrocarbon group may include an alkyl and/or an alkenyl moiety and may contain substituents.
  • One or more hydrogen atoms may be replaced by another atom, for example halogen, or by a non-aliphatic organic group, e.g. an (un)substituted phenyl group, a hydroxy, ether, ketone, aldehyde or ester.
  • a very suitable substituent in the hydrocarbon group is at least one other metal succinate group, yielding a hydrocarbon group having two or more succinate moieties.
  • the aliphatic hydrocarbon group should contain 20 to 200, preferably 35-150, carbon atoms.
  • the chain length is conveniently expressed as the number average molecular weight.
  • the number average molecular weight of the substituent e.g. determined by osmometry, is advantageously from 400 to 2000.
  • the succinic acid derivative may have more than one C 20-200 aliphatic hydrocarbon group attached to one or both alpha-carbon atoms, but preferably it has one C 20-200 aliphatic hydrocarbon group on one of its alpha-carbon atoms and on the other alpha-carbon atom either no substituent or a hydrocarbon of only a short chain length, e.g. C 1-6 group.
  • the latter group can be linked with the C 20-200 hydrocarbon group forming a ring structure.
  • the gasoline compositions of the present invention may also contain one or more detergents.
  • the gasoline composition will comprise a mixture of a major amount of fuel boiling in the gasoline boiling range as described hereinbefore, a minor amount of the furan derivative as defined above and a minor amount of an detergent selected from polyalkenyl amines, e.g. polybutyleneamines, such as "KEROCOM" polyisobutyleneamine, available ex BASF, Mannich amines, polyalkenyl succinimides, poly(oxyalkylene)amines, poly(oxyalkylene) carbamates, poly(alkenyl)-N-substituted carbamates, and mixtures thereof.
  • polyalkenyl amines e.g. polybutyleneamines, such as "KEROCOM" polyisobutyleneamine, available ex BASF, Mannich amines, polyalkenyl succinimides, poly(oxyalkylene)amines, poly(oxyalkylene) carbamates, poly(alkeny
  • the "minor amount" of detergent is preferably less than about 10% by weight of the total fuel composition, more preferably less than about 1% by weight of the total fuel composition and yet more preferably less than about 0.1% by weight of the total fuel composition.
  • the polyalkenyl amine detergents utilised comprise at least one monovalent hydrocarbon group having at least 50 carbon atoms and at least one monovalent hydrocarbon group having at most five carbon atoms bound directly to separate nitrogen atoms of a diamine.
  • Preferred polyalkenyl amines are polyisobutenyl amines. Polyisobutenyl amines are known in the art and representative examples are disclosed in various US Patents including US Patent No. 3,753,670, US Patent No. 3,756,793, US Patent No. 3,574, 576 and US Patent No. 3,438,757.
  • Particularly preferred polyisobutenyl amines for use in the present fuel composition include N-polyisobutenyl-N', N'-dimethyl-1,3-diaminopropane (PIB-DAP), OGA-472 (a polyisobutenyl ethylene diamine available commercially from Oronite), N-polyisobutenyl diethylene triamine (PIB-DETA) and N-polyisobutenyl triethylene tetramine (PIB-TETA) .
  • PIB-DAP N-polyisobutenyl-N', N'-dimethyl-1,3-diaminopropane
  • OGA-472 a polyisobutenyl ethylene diamine available commercially from Oronite
  • PIB-DETA N-polyisobutenyl diethylene triamine
  • PIB-TETA N-polyisobutenyl triethylene tetramine
  • the Mannich amine detergents utilised comprise a condensation product of a high molecular weight alkylsubstituted hydroxyaromatic compound, an amine which contains an amino group having at least one active hydrogen atom (preferably a polyamine), and an aldehyde.
  • a high molecular weight alkylsubstituted hydroxyaromatic compound preferably a polyamine
  • an aldehyde preferably a polyamine
  • Such Mannich amines are known in the art and are disclosed in US Patent No. 4,231,759.
  • the Mannich amine is an alkyl substituted Mannich amine.
  • the polyalkenyl succinimide detergents comprise the reaction product of a dibasic acid anhydride with either a polyoxyalkylene diamine, a hydrocarbyl polyamine or mixtures of both. Typically the succinimide is substituted with the polyalkenyl group but the polyalkenyl group may be found on the polyoxyalkylene diamine or the hydrocarbyl polyamine.
  • Polyalkenyl succinimides are also known in the art and representative examples are disclosed in various patent references including US Patent No. 3,443,918, EP-A-208560, DE-OLS 3,126,404, US Patent No. 4,234,435, US Patent No. 4,810,261, US Patent No. 4,852,993, US Patent No. 4,968,321, US Patent No. 4,985,047, US Patent No. 5,061,291 and US Patent No. 5,147,414.
  • Particularly effective succinimide detergents are those obtained by reacting at least one amine, with a polyalkenyl derivative of a monoethylenically unsaturated C 4-10 dicarboxylic acid material in which the ratio of dicarboxylic acid moieties per polyalkenyl chain is not greater than 1.2:1 and the number average molecular weight (Mn) of the polyalkenyl chain is in the range from 1600 to 5000, e.g. as described in EP-A-587250 (Applicants reference T1665).
  • Amines employed in the preparation of said succinimide detergents are preferably C 1-30 , more preferably C 1-18 , and especially C 8-12 , amines containing 1 to 8 nitrogen atoms.
  • Such amines may be branched or unbranched, saturated aliphatic, primary or secondary amines, containing 1 to 8 nitrogens, preferably mono- or diamines, such as ethylamine, butylamine, sec. butylamine, diethylamine and 3-dimethylamino-1-propylamine, but including higher polyamines such as alkylene polyamines, wherein pairs of nitrogen atoms are joined by alkylene groups of 2 to 4 carbon atoms.
  • Poly(oxyalkylene)amines are described, for example, in US Patents Nos. 4,985,047 and 4,332,595, in EP-A-440 248, EP-A-310 875, EP-A-208 978 and WO-A-85 01956.
  • the poly(oxyalkylene) carbamate detergents comprise an amine moiety and a poly(oxyalkylene) moiety linked together through a carbamate linkage, i.e., -O-C(O)-N ⁇ .
  • poly(oxyalkylene) carbamates are known in the art and representative examples are disclosed for example in US Patent No. 4,191,537, US Patent No. 4,160,648, US Patent No. 4,236,020, US Patent No. 4,270,930, US Patent No. 4,288,612 and US Patent No. 4,881,945.
  • Particularly preferred poly(oxyalkylene) carbamates for use in the present fuel composition include OGA-480 (a poly(oxyalkylene) carbamate which is available commercially from Oronite).
  • the poly(alkenyl)-N-substituted carbamate detergents utilised are of the formula: in which R is a poly(alkenyl) chain; R 1 is a hydrocarbyl or substituted hydrocarbyl group; and A is an N-substituted amino group.
  • R is a poly(alkenyl) chain
  • R 1 is a hydrocarbyl or substituted hydrocarbyl group
  • A is an N-substituted amino group.
  • Poly(alkenyl)-N-substituted carbamates are known in the art and are disclosed in US Patent No. 4,936,868.
  • the one or more detergents are added directly to the fuel boiling in the gasoline boiling range, blended with the furan derivative as defined above, or blended with the furan derivative and one or more carriers before being added to the fuel.
  • the concentration of the one or more detergents in the final fuel composition is generally up to about 1000 ppmw for each detergent.
  • the preferred concentration for each detergent is from about 10 ppmw to about 400 ppmw, based on the total weight of the fuel composition, even more preferably from about 25 ppmw to about 250 ppmw, based on the total weight of the fuel composition.
  • Additive components can be added separately to the fuel boiling in the gasoline boiling range or can be blended with one or more diluents, forming an additive concentrate, and added to the fuel together.
  • Suitable gasoline-compatible diluents are hydrocarbons and mixtures of hydrocarbons with alcohols or ethers, such as methanol, ethanol, propanol, 2-butoxyethanol, methyl tert-butyl ether, or higher alcohols such as "Dobanol 91", (Trade Mark) available from member companies of the Royal Dutch/Shell group.
  • the diluent is an aromatic hydrocarbon solvent such as toluene, xylene, mixtures thereof or mixtures of toluene or xylene with an alcohol.
  • aromatic hydrocarbon solvent such as toluene, xylene, mixtures thereof or mixtures of toluene or xylene with an alcohol.
  • preferred diluents include "Shellsol AB”, “Shellsol R”, (Trade Marks) and low aromatic white spirit (LAWS), which are available from member companies of the Royal Dutch/Shell group.
  • test materials were as follows:
  • N-furfuryl-2-furamide was prepared by adding dropwise to a mixture of furfurylamine (7.44 g; 76 mmol; ex Aldrich) and triethylamine (35.6 g; 352 mmol) in dichloromethane 2-furoyl chloride (23 g; 176 mmol) at a temperature of 0 to 5 °C.
  • the product obtained was washed with water, dried with magnesium sulphate and evaporated. Subsequently, the product so obtained was purified by flash chromatography (silica, hexane/ethyl acetate as eluant) and 14 g (97 % yield) of the product was recovered.
  • Test Material 2 2-amino-1-(2-furanylmethyl)-4,5-difuryl-3-pyrrolecarbonitrile
  • 2-amino-1-(2-furanylmethyl)-4,5-difuryl-3-pyrrolecarbonitrile was prepared as follows: 300 g (1.56 mol) of furoin (ex Aldrich) was reacted with 151.6 g (1.56 mol) of furfurylamine in the presence of 1.5 g of p-toluenesulphonic acid in toluene under stirring at reflux temperature. Water produced by the reaction was removed via a Dean Stark trap. When formation of water had ceased (31 ml removed), 103.1 g (1.56 mol) of malononitrile was added as a dispersion in 100 ml toluene, reflux was continued.
  • N-phenyl furamide was prepared by adding to a mixture of aniline (23.3 g; 250 mmol) and triethylamine (25.3 g; 250 mmol) in dichloromethane slowly 32.6 g (250 mmol) of 2-furoyl chloride, while maintaining the temperature at -10°C.
  • the product obtained was washed with diluted hydrochloric acid and water, dried with magnesium sulphate and evaporated. The product so obtained was than triturated with hexane and filtered. 39.3 g (84 % yield) of product was recovered.
  • Test Material 7 furfuryl alcohol resin, Mn 175
  • a furfuryl alcohol resin of the present invention (Mn 175) was obtained by distilling 100 g of "QuaCorr 1300" furfuryl alcohol resin (Trade Mark) (ex QO Chemicals) (Mn 425) under reduced pressure at a temperature from 42°C (2.24 10 -3 atm) (224 to 92°C (6.58 10 -5 atm) (6.58 Pa)
  • Test Material 8 furfuryl alcohol resin, Mn 156
  • 123 g of a furfuryl alcohol resin of the present invention was obtained by distilling 1,014 g of "QuaCorr 1300" resin (ex QO Chemicals) under reduced pressure at a temperature from 42 °C (7.24 10 -4 atm) (72.4 Pa) to 120 °C (1.97 10 -3 atm) (197 Pa).
  • Test Material 9 Furfuryl alcohol resin, Mn 228
  • 150 g of a furfuryl alcohol resin of the present invention (Mn 228) was prepared by mixing 500 g (5.1 mol) of furfuryl alcohol (ex Aldrich) with 500 g of water and 1.15 g (11.5 mmol) of concentrated sulphuric acid and heating the mixture for 2 hours at a temperature of 50 °C. The mixture so obtained, which separated into two phases, was then neutralised with a saturated sodium bicarbonate solution. The organic phase containing the furfuryl alcohol resin produced was extracted into ether, washed with water, dried with magnesium sulphate and evaporated under reduced pressure.
  • Test Material 10 furfuryl alcohol resin, Mn 272
  • 117 g of a furfuryl alcohol resin of the present invention (Mn 272) was prepared in a manner similar to that described for Test Material 9 except that 400 g (4.1 mol) of the furfuryl alcohol was mixed with 400 g water and 0.092 g (0.92 mmol) of concentrated sulphuric acid, and the mixture was heated for 6 hours at a temperature of from 70 °C to 90°C.
  • Test Material 11 furfuryl alcohol resin, Mn 388
  • 255 g of a furfuryl alcohol resin of the present invention (Mn 388) was prepared in a manner similar to that described for Test Material 10 except that the heating was carried out for 24 hours at a temperature of 50°C, and ten times the amount of concentrated sulphuric acid was used (0.92 g, 9.2 mmol).
  • Test Material 12 esterified furfuryl alcohol resin
  • 321 g of an esterified furfuryl alcohol resin of the present invention was prepared by reacting 150 g (0.42 mol) of Test Material 10 with 176 g (0.42 mol) of C 15 -C 19 internal olefin-succinic anhydride (ex Shell Chemicals) in toluene under reflux for 6 hours, after which the toluene was evaporated.
  • a single cylinder Hydra engine was used, manufactured by Ricardo Co., Shoreham, Hampshire, UK, having bore/stroke 86 mm/86 mm and compression ratio 9.5:1, and fitted with a flat-topped piston and flat-topped cylinder head having two valves.
  • a fuel injector was employed, targeted onto the back of the inlet valve and arranged for injection whilst the valve is closed.
  • the KLSA of the Hydra engine was reduced by between 8 and 10 cad (DKLSA between -8 and -10) over the first 200 hours operation as combustion chamber deposits built up, after which it reached equilibrium. Each additive was tested over a period of continued running, after which the engine was reconditioned on base fuel.
  • the "molecular weight” values for Test Materials 7 to 13 inclusive are number average molecular weight (Mn) values determined by gel permeation chromatography (GPC), using polystyrene calibration standards.
  • a VW engine (1.8 1) modified for research was operated at a speed of 1500 rpm.
  • the deposits were built up at 2250 rpm and a load of 30 Nm.
  • the engine was knock rated by measuring Knock Limited Spark Advance (KLSA) at 1500 rpm and a load of 80 Nm at frequent intervals during the test.
  • KLSA Knock Limited Spark Advance
  • CCD Combustion chamber deposit
  • Example 16 the engine was run for 120 hours using an unleaded gasoline. The engine was then switched to the same gasoline which in addition contained 0.75 g/l of "QuaCorr 1300" furfuryl alcohol resin (ex QO Chemicals) which was dissloved in methylpropanol (0.5% by volume of the gasoline). An increase in KLSA was observed of 2.5 crank angle degrees, after 45 hours when a reference fuel of 85 octane number was used for knock rating. Over the same period of time the CCD weight was reduced from 41.5 mg to 26.6 mg. In other words use of the present additive package established a 36% reduction in CCD weight.
  • Example 17 the engine was run for 43 hours using an unleaded gasoline containing 0.5% by volume of methylpropanol. The engine was then switched to the same gasoline which in addition contained 0.35 g/l of "QuaCorr 1300" furfuryl alcohol resin. An almost immediate increase was observed in KLSA of 3 crank angle degrees, whereas after 43 hours an increase was observed of 1.5 crank angle degrees. Over the same period of time the CCD weight was reduced from 29 mg to 24.5 mg. In other words the use of the present additive established a 16% reduction in CCD weight.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Emergency Medicine (AREA)
  • Combustion & Propulsion (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

This invention provides a fuel composition which comprises a major amount of a fuel boiling in the gasoline boiling range and a minor amount of an additive comprising a furan derivative containing a furyl group bearing one or more substituents comprising one or more heterocyclic and/or one or more aryl groups; an additive concentrate for addition to such fuel and a method of operating an internal combustion engine using such fuel composition. Fuels of the invention give rise to octane requirement increase control and/or octane requirement reduction effects.

Description

  • This invention relates to fuel compositions containing furan derivatives, a method of operating an internal combustion engine using such fuel compositions and to fuel additive concentrates.
  • It is well known in the art that internal combustion engines, more particularly spark ignition engines, tend to exhibit what is termed the octane requirement increase effect. This effect may be described as the tendency for an initially new or relatively clean engine to require higher octane quality fuel as operating time accumulates, and is coincidental with the formation of deposits in the region of the combustion chamber of the engine.
  • During initial operation of a new or clean engine, a gradual increase in octane requirement, i.e. fuel octane number required for knock-free operation, is observed with an increasing build up of combustion chamber deposits until a stable or equilibrium octane requirement level is reached. This level appears to correspond to a point in time when the quantity of deposit accumulation on the combustion chamber and valve surfaces no longer increases but remains relatively constant. This so-called "equilibrium value" is normally reached between 3,000 and 20,000 miles (4,000 and 32,000 km) or corresponding hours of operation. The actual equilibrium value of this increase can vary with engine design and even with individual engines of the same design; however, in almost all cases, the increase appears to be significant, with octane requirement increase values ranging from about 2 to 14 research octane numbers being commonly observed in modern engines.
  • Fuel additives which inhibit or prevent deposit formation in the combustion chamber may be termed octane requirement increase control (ORIC) agents; those which remove or modify formed deposits, leading to decrease in octane requirements, may be termed octane requirement reduction (ORR) agents.
  • US Patent No. 4,339,245 discloses the use of certain furyl compounds including furfuryl alcohol, furfuryl amine, ethylfurfurylacrylate, furfuryl acetate, furfuryl propionate, furfuryl isobutyrate, methyl furoate, ethyl furoate and compounds having alkyl groups substituted on the furyl rings as antiknock additives in gasoline. Addition of the furyl compounds described increased the RON (research octane number) of the gasoline. The RON is an intrinsic property of a gasoline, and is independent of any ORIC or ORR effect which that gasoline might, or might not, manifest in use. No ORIC or ORR activity is either described or hinted at in US Patent No. 4,339,245.
  • EP-A-174 123 discloses a process for the preparation of alkylfurans, and acknowledges that alkylfurans may be included in gasoline compositions as octane improving additives. As above, this relates to the RON of the gasoline, and not to any ORIC or ORR effect.
  • It has now surprisingly been found that fuel compositions containing certain furan derivatives exhibit octane requirement increase control and/or octane requirement reduction effects.
  • According to the present invention there is provided a fuel composition which comprises a major amount of a fuel boiling in the gasoline boiling range and a minor amount of an additive comprising a furan derivative containing a furyl group bearing one or more substituents comprising one or more heterocyclic and/or one or more aryl groups.
  • The or each heterocyclic group may be any optionally substituted saturated or unsaturated ring system, e.g. a 5 to 7 membered ring system, containing at least one heteroatom selected from oxygen, nitrogen and sulphur, 5- and 6-membered rings being preferred, e.g. a furyl, piperidinyl, pyridinyl, pyrrolyl, triazinyl, imidazolinyl or thiophenyl(thienyl) group. Especially preferred are 5-membered ring systems containing oxygen and/or nitrogen, preferably a furan or pyrrole ring.
  • The aryl group(s) may be any optionally substituted aryl group, preferably an optionally-substituted phenyl group. Preferred aryl groups are phenyl groups which are unsubstituted or substituted by an alkyl group.
  • Thus it is preferred that the heterocyclic and/or aryl groups comprise unsaturated 5-membered ring systems containing oxygen and/or nitrogen, or benzene ring systems.
  • Examples of substituent groups for both the heterocyclic and aryl groups include halogen atoms (e.g. chlorine atoms), nitro, hydroxyl, carboxyl, amino, cyano, alkyl, formyl, alkoxycarbonyl, alkanoyl, alkylthio, alkylsulphinyl, alkylsulphonyl, carbamoyl and alkylamido groups. As used herein, when a substituent consists of or contains an alkyl, alkoxy or alkylene moiety, this may be linear or branched and may contain up to 12, preferably up to 6, especially up to 4, carbon atoms.
  • The or each heterocyclic group and/or aryl group is connected to the furyl group directly or by means of a bridging optionally substituted hydrocarbyl (preferably alkylene), carbonyl, dicarbonyl, amido, alkyleneamido, alkyleneoxyalkyl or alkoxycarbonyl group. One or more additional heterocyclic and aryl groups may also be connected to a heterocyclic or aryl group which is connected to the furyl group, directly or via such a bridging group.
  • Preferably connections between furyl groups and heterocyclic or aryl groups as defined above or between heterocyclic or aryl groups and additional heterocyclic or aryl group are either direct connections or are bridging groups selected from C1-4 alkylene (preferably -CH2-), -CH2NHCO-, -NHCO-, -CO-CO-, -CH2-O-CO- and -CH2OCH2- groups.
  • Preferably the furyl group bears a single substituent which comprises one or more heterocyclic and/or one or more aryl groups.
  • For example, the number of heterocyclic and/or aryl groups present in addition in the furyl group may advantageously range from 1 to 5, preferably from 1 to 4.
  • The molecular weight of the furan derivative is preferably in the range from 100 to 5000, more preferably in the range 100 to 500 and most preferably 145 to 500. When the furan derivative is a single compound having a discrete chemical structure, the molecular weight corresponds to the formula weight of the compound. When, however, the furan derivative has a range of structures, the molecular weight is number average molecular weight, as determined by gel permeation chromatography (GPC), using polystyrene calibration standards.
  • By way of example, suitable furan derivatives to be used in accordance with the present invention include those having the following general formula:
    Figure imgb0001
    wherein R1, R2, R3 and R4 each independently represent hydrogen, a heterocyclic group or an aryl group connected to the furyl group directly or by means of a bridging group as defined hereinbefore provided that at least one of R1, R2, R3 and R4 is such a heterocyclic group or an aryl group. Preferably, one or both of R3 and R4 represent an optionally substituted saturated or unsaturated ring system containing at least one heteroatom selected from oxygen, nitrogen and sulphur, connected to the furyl group as defined above.
  • A particularly preferred furan derivative for use in fuel compositions of the present invention is a furfuryl alcohol resin or a derivative thereof.
  • In the context of the present invention a furfuryl alcohol resin is defined as a polymer product obtained by condensation of optionally substituted furfuryl alcohol monomers (e.g. 2-furanmethanol monomers), or a distillation product thereof containing at least two furan rings. Preferably, the furfuryl alcohol resin has a number average molecular weight in the range of 145 (i.e. from about 150) to 5000, more preferably in the range of from 145 (about 150) to 500, as measured by gel permeation chromatography (GPC) using polystyrene calibration standards.
  • It will be understood that the furfuryl alcohol resin or derivative thereof comprises in addition to the furyl group a number of further furyl groups which are connected to the neighbouring furyl groups by means of an optionally substituted hydrocarbyl (preferably alkylene), alkyleneoxyalkyl or alkoxycarbyl group, e.g. a -CH2- or -CH2-O-CH2- group.
  • Preferably, the furfuryl alcohol resin comprises the condensation product of non-substituted 2-furanmethanol monomers.
  • It will be understood that in the latter condensation product the additional furyl groups are connected to the neighbouring furyl groups by means of a methylene group, or in some cases a -CH2-O-CH2-group.
  • The preparation of furfuryl alcohol resins is well known in the art. In this respect reference is for instance made to Journal of Applied Polymer Science, Vol. 15, pp. 1079-1090 (1971), which document is hereby incorporated by reference.
  • Suitable monomers include those having the following general formula:
    Figure imgb0002
    wherein R1, R2, R4 and R5 each independently represent hydrogen, a hydrocarbyl group, a nitrogen-containing, an oxygen-containing or a sulphur-containing hydrocarbyl group and R3 represents hydrogen. The hydrocarbyl group may conveniently comprise an aryl, alkyl, alkenyl or cycloalkyl group. Advantageously, the hydrocarbyl group contains 2 to 50 carbon atoms, preferably 2 to 20 carbon atoms and more preferably 2 to 10 carbon atoms.
  • Suitable furfuryl alcohol resins or derivatives thereof include those obtained by polycondensation of different types of monomers (II).
  • Suitably the furfuryl alcohol resins or derivatives thereof to be applied in accordance with the present invention include those having the following general formulae (III) or (IV):
    Figure imgb0003
    Figure imgb0004
    wherein R1, R2, R3, R4 and R5 have the meanings as defined hereinabove for formula II, R6 represents hydrogen, OH,
    Figure imgb0005
    and R7 and R8 represent an optionally nitrogen-containing, oxygen-containing or sulphur-containing hydrocarbyl group, x is in the range from 0 to 60, preferably from 0 to 30 and more preferably from 0 to 10, y is 0 or 1, z is in the range from 0 to 60, preferably from 0 to 30 and more preferably from 0 to 10, each of (x + z) and Z' ranges from 1 to 60, preferably 1 to 30 and more preferably from 1 to 10, and p is in the range from 1 to 80, preferably ranging from 5 to 25.
  • It will be understood that the furfuryl alcohol resin or derivatives thereof will usually comprise a mixture of any of the polymer products III and IV described above, and of course any unreacted 2-furanmethanol or derivative thereof.
  • The furfuryl alcohol resins may contain unreacted hydroxy groups which may subsequently be derivatised, e.g. esterified, in known manner. A preferred derivative is an alkylsuccinic acid ester of a furfuryl resin, which may be prepared by reaction of the furfuryl resin with an olefin-succinic anhydride, e.g. a C15-19 internal olefin-succinic anhydride.
  • A particularly preferred fuel composition according to the present invention is one wherein the furan derivative is selected from the group consisting of N-furfuryl-2-furamide, 2-amino-1-(2-furanylmethyl)-4,5-difuryl-3-pyrrolecarbonitrile, N-phenyl furamide, 1-furfurylpyrrole, furil, furfuryl benzoate, furfuryl resins having number average molecular weights in the range 145 to 500 and alkylsuccinic acid esters of furfuryl resins having number average molecular weights in said range.
  • The additive comprising the furan derivative is preferably present in the fuel composition in an octane requirement reducing amount.
  • The fuel is present in a major amount (i.e. more than 50%w), and the additive comprising the furan derivative is present in a minor amount, preferably from 0.005 to 10%w, more preferably from 0.01 to 5%w, and most preferably from 0.02 to 1%w, based on the weight of the fuel composition.
  • The invention further provides an additive concentrate suitable for addition to fuel for an internal combustion engine which comprises a fuel-compatible diluent and an additive comprising a furan derivative as defined above, preferably in an amount of from 5 to 75%w calculated on the diluent.
  • Further in accordance with the present invention there is provided a method of operating an internal combustion engine which comprises introducing into the combustion chambers of said engine a fuel composition as defined above according to the invention.
  • The fuel boiling in the gasoline boiling range may consist substantially of hydrocarbons or it may contain blending components. Alternatively, e.g. in countries such as Brazil, the fuel may consist substantially of ethanol.
  • Suitable liquid hydrocarbon fuels of the gasoline boiling range are mixtures of hydrocarbon boiling in the temperature range from about 25°C to about 232°C, and comprise mixtures of saturated hydrocarbons, olefinic hydrocarbons and aromatic hydrocarbons. Preferred are gasoline mixtures having a saturated hydrocarbon content ranging from about 40% to about 80% by volume, an olefinic hydrocarbon content from 0% to about 30% by volume and an aromatic hydrocarbon content from about 10% to about 60% by volume. The base fuel is derived from straight run gasoline, polymer gasoline, natural gasoline, dimer and trimerized olefins, synthetically produced aromatic hydrocarbon mixtures, from thermally or catalytically reformed hydrocarbons, or from catalytically cracked or thermally cracked petroleum stocks, and mixtures of these. The hydrocarbon composition and octane level of the base fuel are not critical. The octane level, (R+M)/2, will generally be above about 85 (where R is Research Octane Number and M is Motor Octane Number).
  • Any conventional base gasoline can be employed in the practice of the present invention. For example, hydrocarbons in the gasoline can be replaced by up to a substantial amount of conventional alcohols or ethers, conventionally known for use in fuels. The base gasolines are desirably substantially free of water since water could impede a smooth combustion.
  • Normally, the gasolines to which the invention is applied may be leaded or unleaded, although are preferably substantially lead-free, and may contain minor amounts of one or more blending agents such as methanol, ethanol, tertiary butanol, ethyl tertiary butyl ether, methyl tertiary butyl ether, and the like, at from about 0.1% by volume to about 25% by volume of the base fuel, although larger amounts (e.g. up to 40%v) may be utilised.
  • The gasolines may further suitably contain a nonionic surfactant, such as an alkylphenol or an alkyl alkoxylate. Suitable examples of such surfactants include C4-C18-alkylphenol and C2-C6-alkylethoxylate or C2-C6-alkylpropoxylate or mixtures thereof. The amount of the surfactant is advantageously from 10 to 1000 ppmw.
  • The gasoline can also contain other conventional additives including antioxidants such as phenolics, e.g. 2,6-di-tert-butylphenol or phenylenediamines, e.g. N,N'-di-sec-butyl-p-phenylenediamine, dyes, metal deactivators, dehazers such as polyester-type ethoxylated alkylphenol-formaldehyde resins. Corrosion inhibitors, such as that commercially sold by Rhein Chemie, Mannheim, Germany as "RC 4801", or a polyhydric alcohol ester of a succinic acid derivative having on at least one of its alpha-carbon atoms an unsubstituted or substituted aliphatic hydrocarbon group having from 20 to 500 carbon atoms, for example, pentaerythritol diester of polyisobutylene-substituted succinic acid, the polyisobutylene group having an average molecular weight of about 950, in an amount from about 1 ppmw to about 1000 ppmw, may also be present. The fuels can also contain antiknock compounds such as methyl cyclopentadienylmanganese tricarbonyl, tetraethyl lead or other lead-containing compounds, and ortho-azodiphenol as well as co-antiknock compounds such as benzoyl acetone.
  • A preferred gasoline composition of the invention may additionally contain a minor amount of at least one additional additive compound selected from the group consisting of polyalkenyl amines, Mannich amines, polyalkenyl succinimide, poly(oxyalkylene)amines, poly(oxyalkylene)carbamates, and poly(alkenyl)-N-substituted carbamates.
  • An effective amount of the additive comprising the furan derivative is introduced into the combustion zone of the engine in a variety of ways to prevent build-up of deposits or to accomplish the modification of existing deposits that are related to octane requirement. A preferred method is to add a minor amount of a furan derivative as defined above to the gasoline. For example, one or more furan derivatives as defined above are added directly to the gasoline or are blended with one or more carriers and/or one or more hydrocarbon-soluble alkali metal or alkaline earth metal salts and/or one or more additional detergents before being added to the gasoline.
  • The amount of furan derivative used will depend on the particular furan derivative used, the fuel, and the presence or absence of carriers, detergents and diluents.
  • The carrier, when utilised, may conveniently have an average molecular weight from about 250 to about 5000. Suitable carriers, when utilised, include hydrocarbon based materials such as polyisobutylenes (PIB's), polypropylenes (PP's) and polyalphaolefins (PAO's), all of which may be hydrogenated or unhydrogenated but are preferably hydrogenated; polyether based materials such as polybutylene oxides (poly BO's), polypropylene oxides (poly PO's), polyhexadecene oxides (poly HO's) and mixtures thereof (i.e. both (poly BO) + (poly PO) and poly-BO-PO)); and mineral oils such as those sold by member companies of the Royal Dutch/Shell group under the designations "HVI" and "XHVI" (trade mark), Exxon Naphthenic 900 sus mineral oil and high viscosity index oils in general. The carrier is preferably selected from PIB's, poly BO's and poly PO's with poly PO's being the most preferred.
  • A particularly prepared carrier fluid comprises a combination of a polyalphaolefin having a viscosity at 100°C in the range 2 x 10-6 to 2 x 10-5 m2/s (2 to 20 centistokes) being a hydrogenated oligomer containing 18 to 80 carbon atoms derived from at least one alphaolefinic monomer containing from 8 to 16 carbon atoms, and a polyoxyalkylene compound selected from glycols, mono- and diethers thereof, having number average molecular weight (Mn) in the range 400 to 3000, the weight ratio polyalphaolefin: polyoxyalkylene compound being in the range 1:10 to 10:1.
  • The polyalphaolefins are primarily trimers, tetramers and pentamers, and synthesis of such materials is outlined in Campen et al., "Growing use of synlubes", Hydrocarbon Processing, February 1982, pages 75 to 82. The polyalphaolefin is preferably derived from an alphaolefinic monomer containing from 8 to 12 carbon atoms. Polyalphaolefins derived from decene-1 have been found to be very effective. The polyalphaolefin preferably has viscosity at 100°C in the range of 6 x 10-6 to 1 x 10-5 m2/s (6 to 10 centistokes). Polyalphaolefin having a viscosity at 100°C of 8 x 10-6 m2/s (8 centistokes) has been found to be very effective.
  • Preferred polyoxyalkylene compounds for use in combination with these polyalphaolefins are described in EP-A-588429 (Applicants reference T 5677).
  • The carrier concentration in the final fuel composition is up to about 1000 ppm weight. When a carrier is present, the preferred concentration is from about 50 ppm by weight to about 400 ppm by weight, based on the total weight of the fuel composition. Once the carrier is blended with the furan derivative and any other desired components, the blend is added directly to the fuel or packaged for future use.
  • The hydrocarbon-soluble alkali metal or alkaline earth metal salt, when utilised, may be one of those described in WO 87/01126, and the compounds of formula I are particularly suitable for incorporation, as additional component, in fuel compositions as described in WO 87/01126. Preferred hydrocarbon-soluble alkali metal or alkaline earth metal salts are, however, alkali metal or alkaline earth metal salts of a succinic acid derivative. Such a salt of a succinic acid derivative, when utilised, will have as a substituent on one of its alpha-carbon atoms an unsubstituted or substituted aliphatic hydrocarbon group having from 20 to 200 carbon atoms.
  • Alternatively, the succinic acid derivative will have as a substituent on one of its alpha-carbon atoms an unsubstituted or substituted hydrocarbon group having from 20 to 200 carbon atoms which is connected to the other alpha-carbon atom by means of a hydrocarbon moiety having from 1 to 6 carbon atoms, forming a ring structure. Suitable such salts are described for example in EP-A-207560 and in EP-A-491439.
  • The salts of the succinic acid derivative can be monobasic or dibasic. Monobasic salts in which the remaining carboxylic acid group has been transformed into an amide or ester group may also be used. Suitable alkali metal salts of a partial ester of an alkyl polyether alcohol with a succinic acid derivative are described in EP-A-491439.
  • Suitable metal salts include lithium, sodium, potassium, rubidium, caesium and calcium salts. Particularly preferred salts are described in EP-A-207560.
  • The aliphatic hydrocarbon substituent(s) of the succinic acid derivative is suitably derived from a polyolefin, the monomers of which have 2 to 6 carbon atoms. Thus, convenient substituents include polyethylene, polypropylene, polybutylenes, polypentenes, polyhexenes or mixed polymers. Particularly preferred is an aliphatic hydrocarbon group which is derived from polyisobutylene.
  • The hydrocarbon group may include an alkyl and/or an alkenyl moiety and may contain substituents. One or more hydrogen atoms may be replaced by another atom, for example halogen, or by a non-aliphatic organic group, e.g. an (un)substituted phenyl group, a hydroxy, ether, ketone, aldehyde or ester. A very suitable substituent in the hydrocarbon group is at least one other metal succinate group, yielding a hydrocarbon group having two or more succinate moieties.
  • The aliphatic hydrocarbon group should contain 20 to 200, preferably 35-150, carbon atoms. When a polyolefin is used as substituent the chain length is conveniently expressed as the number average molecular weight. The number average molecular weight of the substituent, e.g. determined by osmometry, is advantageously from 400 to 2000.
  • The succinic acid derivative may have more than one C20-200 aliphatic hydrocarbon group attached to one or both alpha-carbon atoms, but preferably it has one C20-200 aliphatic hydrocarbon group on one of its alpha-carbon atoms and on the other alpha-carbon atom either no substituent or a hydrocarbon of only a short chain length, e.g. C1-6 group. The latter group can be linked with the C20-200 hydrocarbon group forming a ring structure.
  • The gasoline compositions of the present invention may also contain one or more detergents. When detergents are utilised, the gasoline composition will comprise a mixture of a major amount of fuel boiling in the gasoline boiling range as described hereinbefore, a minor amount of the furan derivative as defined above and a minor amount of an detergent selected from polyalkenyl amines, e.g. polybutyleneamines, such as "KEROCOM" polyisobutyleneamine, available ex BASF, Mannich amines, polyalkenyl succinimides, poly(oxyalkylene)amines, poly(oxyalkylene) carbamates, poly(alkenyl)-N-substituted carbamates, and mixtures thereof. As noted above, a carrier as described hereinbefore may also be included. The "minor amount" of detergent is preferably less than about 10% by weight of the total fuel composition, more preferably less than about 1% by weight of the total fuel composition and yet more preferably less than about 0.1% by weight of the total fuel composition.
  • The polyalkenyl amine detergents utilised comprise at least one monovalent hydrocarbon group having at least 50 carbon atoms and at least one monovalent hydrocarbon group having at most five carbon atoms bound directly to separate nitrogen atoms of a diamine. Preferred polyalkenyl amines are polyisobutenyl amines. Polyisobutenyl amines are known in the art and representative examples are disclosed in various US Patents including US Patent No. 3,753,670, US Patent No. 3,756,793, US Patent No. 3,574, 576 and US Patent No. 3,438,757. Particularly preferred polyisobutenyl amines for use in the present fuel composition include N-polyisobutenyl-N', N'-dimethyl-1,3-diaminopropane (PIB-DAP), OGA-472 (a polyisobutenyl ethylene diamine available commercially from Oronite), N-polyisobutenyl diethylene triamine (PIB-DETA) and N-polyisobutenyl triethylene tetramine (PIB-TETA) .
  • The Mannich amine detergents utilised comprise a condensation product of a high molecular weight alkylsubstituted hydroxyaromatic compound, an amine which contains an amino group having at least one active hydrogen atom (preferably a polyamine), and an aldehyde. Such Mannich amines are known in the art and are disclosed in US Patent No. 4,231,759. Preferably, the Mannich amine is an alkyl substituted Mannich amine.
  • The polyalkenyl succinimide detergents comprise the reaction product of a dibasic acid anhydride with either a polyoxyalkylene diamine, a hydrocarbyl polyamine or mixtures of both. Typically the succinimide is substituted with the polyalkenyl group but the polyalkenyl group may be found on the polyoxyalkylene diamine or the hydrocarbyl polyamine. Polyalkenyl succinimides are also known in the art and representative examples are disclosed in various patent references including US Patent No. 3,443,918, EP-A-208560, DE-OLS 3,126,404, US Patent No. 4,234,435, US Patent No. 4,810,261, US Patent No. 4,852,993, US Patent No. 4,968,321, US Patent No. 4,985,047, US Patent No. 5,061,291 and US Patent No. 5,147,414.
  • Particularly effective succinimide detergents are those obtained by reacting at least one amine, with a polyalkenyl derivative of a monoethylenically unsaturated C4-10 dicarboxylic acid material in which the ratio of dicarboxylic acid moieties per polyalkenyl chain is not greater than 1.2:1 and the number average molecular weight (Mn) of the polyalkenyl chain is in the range from 1600 to 5000, e.g. as described in EP-A-587250 (Applicants reference T1665).
  • Amines employed in the preparation of said succinimide detergents are preferably C1-30, more preferably C1-18, and especially C8-12, amines containing 1 to 8 nitrogen atoms. Such amines may be branched or unbranched, saturated aliphatic, primary or secondary amines, containing 1 to 8 nitrogens, preferably mono- or diamines, such as ethylamine, butylamine, sec. butylamine, diethylamine and 3-dimethylamino-1-propylamine, but including higher polyamines such as alkylene polyamines, wherein pairs of nitrogen atoms are joined by alkylene groups of 2 to 4 carbon atoms.
  • Poly(oxyalkylene)amines are described, for example, in US Patents Nos. 4,985,047 and 4,332,595, in EP-A-440 248, EP-A-310 875, EP-A-208 978 and WO-A-85 01956. The poly(oxyalkylene) carbamate detergents comprise an amine moiety and a poly(oxyalkylene) moiety linked together through a carbamate linkage, i.e., -O-C(O)-N<.
  • These poly(oxyalkylene) carbamates are known in the art and representative examples are disclosed for example in US Patent No. 4,191,537, US Patent No. 4,160,648, US Patent No. 4,236,020, US Patent No. 4,270,930, US Patent No. 4,288,612 and US Patent No. 4,881,945. Particularly preferred poly(oxyalkylene) carbamates for use in the present fuel composition include OGA-480 (a poly(oxyalkylene) carbamate which is available commercially from Oronite).
  • The poly(alkenyl)-N-substituted carbamate detergents utilised are of the formula:
    Figure imgb0006
    in which R is a poly(alkenyl) chain; R1 is a hydrocarbyl or substituted hydrocarbyl group; and A is an N-substituted amino group. Poly(alkenyl)-N-substituted carbamates are known in the art and are disclosed in US Patent No. 4,936,868.
  • The one or more detergents are added directly to the fuel boiling in the gasoline boiling range, blended with the furan derivative as defined above, or blended with the furan derivative and one or more carriers before being added to the fuel.
  • The concentration of the one or more detergents in the final fuel composition is generally up to about 1000 ppmw for each detergent. When one or more detergents are utilised, the preferred concentration for each detergent is from about 10 ppmw to about 400 ppmw, based on the total weight of the fuel composition, even more preferably from about 25 ppmw to about 250 ppmw, based on the total weight of the fuel composition.
  • Additive components can be added separately to the fuel boiling in the gasoline boiling range or can be blended with one or more diluents, forming an additive concentrate, and added to the fuel together. Suitable gasoline-compatible diluents are hydrocarbons and mixtures of hydrocarbons with alcohols or ethers, such as methanol, ethanol, propanol, 2-butoxyethanol, methyl tert-butyl ether, or higher alcohols such as "Dobanol 91", (Trade Mark) available from member companies of the Royal Dutch/Shell group.
  • Preferably the diluent is an aromatic hydrocarbon solvent such as toluene, xylene, mixtures thereof or mixtures of toluene or xylene with an alcohol. Additionally preferred diluents include "Shellsol AB", "Shellsol R", (Trade Marks) and low aromatic white spirit (LAWS), which are available from member companies of the Royal Dutch/Shell group.
  • Use in fuels of the preferred furan derivatives of the present invention, especially preferred furfuryl alcohol resins, in concentrations within the preferred ranges has been found to bring about considerable reduction in combustion chamber deposit weights. From observations, it is believed that this is achieved by promotion of deposit flaking in combustion chambers.
  • The present invention will be further understood from the following illustrative examples, in which the test materials were as follows:-
  • Test Material 1 - N-furfuryl-2-furamide
  • N-furfuryl-2-furamide was prepared by adding dropwise to a mixture of furfurylamine (7.44 g; 76 mmol; ex Aldrich) and triethylamine (35.6 g; 352 mmol) in dichloromethane 2-furoyl chloride (23 g; 176 mmol) at a temperature of 0 to 5 °C. The product obtained was washed with water, dried with magnesium sulphate and evaporated. Subsequently, the product so obtained was purified by flash chromatography (silica, hexane/ethyl acetate as eluant) and 14 g (97 % yield) of the product was recovered.
  • Test Material 2 - 2-amino-1-(2-furanylmethyl)-4,5-difuryl-3-pyrrolecarbonitrile
  • 2-amino-1-(2-furanylmethyl)-4,5-difuryl-3-pyrrolecarbonitrile was prepared as follows: 300 g (1.56 mol) of furoin (ex Aldrich) was reacted with 151.6 g (1.56 mol) of furfurylamine in the presence of 1.5 g of p-toluenesulphonic acid in toluene under stirring at reflux temperature. Water produced by the reaction was removed via a Dean Stark trap. When formation of water had ceased (31 ml removed), 103.1 g (1.56 mol) of malononitrile was added as a dispersion in 100 ml toluene, reflux was continued. When again formation of water had ceased (26 ml removed via the Dean Stark trap), the reaction mixture was cooled and the toluene was removed by evaporation. In this way 498 g of a black solid product was obtained. Subsequently, 100 g of this product was purified by flash chromatography (silica, hexane/ethyl acetate as eluant) and 24 g of the product was recovered.
  • Test Material 3 - N-phenyl furamide
  • N-phenyl furamide was prepared by adding to a mixture of aniline (23.3 g; 250 mmol) and triethylamine (25.3 g; 250 mmol) in dichloromethane slowly 32.6 g (250 mmol) of 2-furoyl chloride, while maintaining the temperature at -10°C. The product obtained was washed with diluted hydrochloric acid and water, dried with magnesium sulphate and evaporated. The product so obtained was than triturated with hexane and filtered. 39.3 g (84 % yield) of product was recovered.
  • Test Material 4 - 1-furfurylpyrrole (ex Aldrich) Test Material 5 - furil (ex Aldrich) Test Material 6 - furfuryl benzoate (ex Aldrich) Test Material 7 - furfuryl alcohol resin, Mn 175
  • 10.6 g of a furfuryl alcohol resin of the present invention (Mn 175) was obtained by distilling 100 g of "QuaCorr 1300" furfuryl alcohol resin (Trade Mark) (ex QO Chemicals) (Mn 425) under reduced pressure at a temperature from 42°C (2.24 10-3 atm) (224 to 92°C (6.58 10-5 atm) (6.58 Pa)
  • Test Material 8 - furfuryl alcohol resin, Mn 156
  • 123 g of a furfuryl alcohol resin of the present invention (Mn 156) was obtained by distilling 1,014 g of "QuaCorr 1300" resin (ex QO Chemicals) under reduced pressure at a temperature from 42 °C (7.24 10-4 atm) (72.4 Pa) to 120 °C (1.97 10-3 atm) (197 Pa).
  • Test Material 9 - Furfuryl alcohol resin, Mn 228
  • 150 g of a furfuryl alcohol resin of the present invention (Mn 228) was prepared by mixing 500 g (5.1 mol) of furfuryl alcohol (ex Aldrich) with 500 g of water and 1.15 g (11.5 mmol) of concentrated sulphuric acid and heating the mixture for 2 hours at a temperature of 50 °C. The mixture so obtained, which separated into two phases, was then neutralised with a saturated sodium bicarbonate solution. The organic phase containing the furfuryl alcohol resin produced was extracted into ether, washed with water, dried with magnesium sulphate and evaporated under reduced pressure.
  • Test Material 10 - furfuryl alcohol resin, Mn 272
  • 117 g of a furfuryl alcohol resin of the present invention (Mn 272) was prepared in a manner similar to that described for Test Material 9 except that 400 g (4.1 mol) of the furfuryl alcohol was mixed with 400 g water and 0.092 g (0.92 mmol) of concentrated sulphuric acid, and the mixture was heated for 6 hours at a temperature of from 70 °C to 90°C.
  • Test Material 11 - furfuryl alcohol resin, Mn 388
  • 255 g of a furfuryl alcohol resin of the present invention (Mn 388) was prepared in a manner similar to that described for Test Material 10 except that the heating was carried out for 24 hours at a temperature of 50°C, and ten times the amount of concentrated sulphuric acid was used (0.92 g, 9.2 mmol).
  • Test Material 12 - esterified furfuryl alcohol resin
  • 321 g of an esterified furfuryl alcohol resin of the present invention was prepared by reacting 150 g (0.42 mol) of Test Material 10 with 176 g (0.42 mol) of C15-C19 internal olefin-succinic anhydride (ex Shell Chemicals) in toluene under reflux for 6 hours, after which the toluene was evaporated.
  • Test Material 13 - "Quacorr 1300" furfuryl alcohol resin (ex QO Chemicals, Sheffield, UK) (Mn 425) Comparative Test Material A - 2 - furaldehyde diethyl-(Comp. A) acetal (ex Aldrich) Comparative Test Material B - 2-furaldehyde dimethyl-(Comp. B) hydrazone (ex Aldrich) Comparative Test Material C - furfuryl alcohol (ex (Comp. C) Aldrich)
  • In each of the examples which follow, samples of the test materials were dissolved in unleaded gasoline and the resulting fuels (gasoline compositions) were tested as will be described.
  • EXAMPLES 1 to 5
  • The beneficial effect on octane requirement of gasoline additives comprising furan derivatives in accordance with the present invention was demonstrated by the following procedure.
  • A single cylinder Hydra engine was used, manufactured by Ricardo Co., Shoreham, Sussex, UK, having bore/stroke 86 mm/86 mm and compression ratio 9.5:1, and fitted with a flat-topped piston and flat-topped cylinder head having two valves. A fuel injector was employed, targeted onto the back of the inlet valve and arranged for injection whilst the valve is closed.
  • Deposits were built up at 1000 rpm with wide open throttle (WOT) and high load during 200 hours with an unleaded gasoline containing 0.5 wt% fluoranthene. Cylinder pressure signals were monitored to detect the high rate of change in cylinder pressure during autoignition and Knock Limited Spark Advance (KLSA) was determined under 1000 rpm and WOT conditions. Calibration tests with reference fuels showed that the engine responded to the Research Octane Number (RON) of the fuel and that the KLSA changed by approximately one crank angle degree (cad) per octane number. Starting from clean combustion chamber conditions, the KLSA of the Hydra engine was reduced by between 8 and 10 cad (DKLSA between -8 and -10) over the first 200 hours operation as combustion chamber deposits built up, after which it reached equilibrium. Each additive was tested over a period of continued running, after which the engine was reconditioned on base fuel.
  • The various properties of the additives, conditions applied and results of the experiments are shown in Table 1. It will be clear from these results that the use of the test materials 1 to 13 in accordance with the present invention (Examples 1 to 15) brings about a surprisingly high reduction in the octane requirement of the engine when compared with the comparative test materials A, B and C falling outside the scope of the present invention (Comparative Examples A, B and C).
    Figure imgb0007
  • The "molecular weight" values for Test Materials 7 to 13 inclusive are number average molecular weight (Mn) values determined by gel permeation chromatography (GPC), using polystyrene calibration standards.
  • Examples 16 and 17
  • In two further experiments a VW engine (1.8 1) modified for research was operated at a speed of 1500 rpm. The deposits were built up at 2250 rpm and a load of 30 Nm. The engine was knock rated by measuring Knock Limited Spark Advance (KLSA) at 1500 rpm and a load of 80 Nm at frequent intervals during the test. Combustion chamber deposit (CCD) weight was monitored by stopping the engine and removing two plugs from the combustion chamber.
  • In Example 16, the engine was run for 120 hours using an unleaded gasoline. The engine was then switched to the same gasoline which in addition contained 0.75 g/l of "QuaCorr 1300" furfuryl alcohol resin (ex QO Chemicals) which was dissloved in methylpropanol (0.5% by volume of the gasoline). An increase in KLSA was observed of 2.5 crank angle degrees, after 45 hours when a reference fuel of 85 octane number was used for knock rating. Over the same period of time the CCD weight was reduced from 41.5 mg to 26.6 mg. In other words use of the present additive package established a 36% reduction in CCD weight.
  • In Example 17, the engine was run for 43 hours using an unleaded gasoline containing 0.5% by volume of methylpropanol. The engine was then switched to the same gasoline which in addition contained 0.35 g/l of "QuaCorr 1300" furfuryl alcohol resin. An almost immediate increase was observed in KLSA of 3 crank angle degrees, whereas after 43 hours an increase was observed of 1.5 crank angle degrees. Over the same period of time the CCD weight was reduced from 29 mg to 24.5 mg. In other words the use of the present additive established a 16% reduction in CCD weight.

Claims (10)

  1. A fuel composition which comprises a major amount of a fuel boiling in the gasoline boiling range and a minor amount of an additive comprising a furan derivative containing a furyl group bearing one or more substituents comprising one or more heterocyclic and/or one or more aryl groups.
  2. A fuel composition according to Claim 1 wherein the heterocyclic and/or aryl groups comprise unsaturated 5-membered ring systems containing oxygen and/or nitrogen or benzene ring systems.
  3. A fuel composition according to claim 1, wherein the furyl group bears a single substituent which comprises one or more heterocyclic and/or one or more aryl groups.
  4. A fuel composition according to claim 1, 2 or 3, wherein the molecular weight of the furan derivative is in the range from 100 to 5000.
  5. A fuel composition according to any one of claims 1 to 4 wherein the furan derivative is a furfuryl alcohol resin having a number average molecular weight in the range from 145 to 5000.
  6. A fuel composition according to any one of Claims 1 to 5, wherein the furan derivative has a molecular weight in the range of 145 to 500.
  7. A fuel composition according to any one of Claims 1 to 4 wherein the furan derivative is selected from the group consisting of N-furfuryl-2-furamide, 2-amino-1-(2-furanylmethyl)-4,5-difuryl-3-pyrrolecarbonitrile, N-phenyl furamide, 1-furfurylpyrrole, furil, furfuryl benzoate, furfuryl resins having number average molecular weights in the range 145 to 500 and alkylsuccinic acid esters of furfuryl resins having number average molecular weights in said range.
  8. A fuel composition according to any one of Claims 1 to 7 wherein the furan derivative is present in an octane requirement reducing amount.
  9. An additive concentrate suitable for addition to fuel for an internal combustion engine which comprises a fuel-compatible diluent and an additive comprising a furan derivative as defined in any one of claims 1 to 8.
  10. A method of operating an internal combustion engine which comprises introducing into the combustion chambers of said engine a fuel composition according to any one of claims 1 to 8.
EP97200775A 1996-03-15 1997-03-14 Fuel compositions Expired - Lifetime EP0795596B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP97200775A EP0795596B1 (en) 1996-03-15 1997-03-14 Fuel compositions

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
EP96301782 1996-03-15
EP96301782 1996-03-15
EP96301781 1996-03-15
EP96301781 1996-03-15
EP97200775A EP0795596B1 (en) 1996-03-15 1997-03-14 Fuel compositions

Publications (2)

Publication Number Publication Date
EP0795596A1 true EP0795596A1 (en) 1997-09-17
EP0795596B1 EP0795596B1 (en) 2000-10-11

Family

ID=27237695

Family Applications (1)

Application Number Title Priority Date Filing Date
EP97200775A Expired - Lifetime EP0795596B1 (en) 1996-03-15 1997-03-14 Fuel compositions

Country Status (1)

Country Link
EP (1) EP0795596B1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP2034005A1 (en) * 2007-09-07 2009-03-11 Furanix Technologies B.V Fuel additive concentrate derived from a biomass resource
US20160009652A1 (en) * 2007-03-30 2016-01-14 University Of Rochester Small-molecule modulators of melanin expression

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE575147C (en) * 1931-06-06 1933-04-25 Ethyl Gasoline Corp Carbon removers for internal combustion engines
GB392998A (en) * 1931-06-06 1933-06-01 Ethyl Gasoline Corp Improvements in or relating to the removal of carbon deposits from the cylinders of internal combustion engines
DE671891C (en) * 1932-05-26 1939-02-16 John Westley Orelup Process for preventing gum formation in gum-prone gasolines and other petroleum distillates
US2535058A (en) * 1947-03-03 1950-12-26 Universal Oil Prod Co Stabilization process
US2554687A (en) * 1948-01-29 1951-05-29 Universal Oil Prod Co Stabilization of organic compounds
GB795067A (en) * 1955-08-11 1958-05-14 Shell Res Ltd Liquid fuel for internal combustion engines
GB802589A (en) * 1955-03-22 1958-10-08 California Research Corp Compounded hydrocarbon fuels
FR1284977A (en) * 1960-03-29 1962-02-16 Shell Int Research Fuel composition
US3277056A (en) * 1963-11-27 1966-10-04 Lubrizol Corp N-3-oxohydrocarbon-substituted acrylamides and polymers thereof
GB1116227A (en) * 1964-10-02 1968-06-06 Rohm & Haas Fuel and lubricant compositions
US5196035A (en) * 1991-09-20 1993-03-23 Shell Oil Company Gasoline composition for reducing intake valve deposits in port fuel injected engines
GB2293177A (en) * 1994-09-02 1996-03-20 Ass Octel Gasoline compositions containing carbamates

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE575147C (en) * 1931-06-06 1933-04-25 Ethyl Gasoline Corp Carbon removers for internal combustion engines
GB392998A (en) * 1931-06-06 1933-06-01 Ethyl Gasoline Corp Improvements in or relating to the removal of carbon deposits from the cylinders of internal combustion engines
DE671891C (en) * 1932-05-26 1939-02-16 John Westley Orelup Process for preventing gum formation in gum-prone gasolines and other petroleum distillates
US2535058A (en) * 1947-03-03 1950-12-26 Universal Oil Prod Co Stabilization process
US2554687A (en) * 1948-01-29 1951-05-29 Universal Oil Prod Co Stabilization of organic compounds
GB802589A (en) * 1955-03-22 1958-10-08 California Research Corp Compounded hydrocarbon fuels
GB795067A (en) * 1955-08-11 1958-05-14 Shell Res Ltd Liquid fuel for internal combustion engines
FR1284977A (en) * 1960-03-29 1962-02-16 Shell Int Research Fuel composition
US3277056A (en) * 1963-11-27 1966-10-04 Lubrizol Corp N-3-oxohydrocarbon-substituted acrylamides and polymers thereof
GB1116227A (en) * 1964-10-02 1968-06-06 Rohm & Haas Fuel and lubricant compositions
US5196035A (en) * 1991-09-20 1993-03-23 Shell Oil Company Gasoline composition for reducing intake valve deposits in port fuel injected engines
GB2293177A (en) * 1994-09-02 1996-03-20 Ass Octel Gasoline compositions containing carbamates

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20160009652A1 (en) * 2007-03-30 2016-01-14 University Of Rochester Small-molecule modulators of melanin expression
EP2034005A1 (en) * 2007-09-07 2009-03-11 Furanix Technologies B.V Fuel additive concentrate derived from a biomass resource

Also Published As

Publication number Publication date
EP0795596B1 (en) 2000-10-11

Similar Documents

Publication Publication Date Title
EP0897382B1 (en) Alkoxy acetic acid derivatives
US5749929A (en) Fuel additive compositions containing aromatic esters of polyalkylphenoxyalkanols and poly (oxyalkylene) amines
EP0721010A1 (en) Fuel compositions containing aryl succinimides
EP0658573B1 (en) Mannich condensation products of polyalkylene hydroxyaromatic esters and fuel compositions containing the same
AU690183B2 (en) Polyalkyl nitro and amino aromatic esters and fuel compositions containing the same
EP0491439A1 (en) Gasoline composition
EP0795596B1 (en) Fuel compositions
AU726632B2 (en) Fuel compositions
EP1274820B1 (en) Fuel oil compositions
CA2255519A1 (en) Fuel compositions containing polyamines of polyalkyl aromatic esters
US5466268A (en) Polyalkyl and polyalkenyl aromatic amides and fuel compositions containing the same
AU714834B2 (en) Fuel additive compositions containing aromatic esters of polyalkylphenoxyalkanols and poly(oxyalkylene) amines
MXPA97001875A (en) Combustib compositions
CA2287766C (en) Fuel additive compositions containing aromatic esters of polyalkylphenoxyalkanols and aliphatic amines
EP0781785B1 (en) Polyalkylphenyl and polyalkyloxycarbonylphenyl amino and nitro benzoates and fuel compositions containing the same
US5728182A (en) Polyalkyl esters of substituted polyphenyl ethers and fuel compositions containing the same
CN115725347A (en) Mannich-based quaternary ammonium salt fuel additives
CN115725348A (en) Mannich-based quaternary ammonium salt fuel additives
MXPA98000312A (en) Compositions additives for fuel containing aromatic esters of polyalquylphenoxialcanols and poly (oxialquilen) ami

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): BE CH DE ES FI FR GB IT LI NL

17P Request for examination filed

Effective date: 19980121

17Q First examination report despatched

Effective date: 19990406

GRAG Despatch of communication of intention to grant

Free format text: ORIGINAL CODE: EPIDOS AGRA

GRAG Despatch of communication of intention to grant

Free format text: ORIGINAL CODE: EPIDOS AGRA

GRAG Despatch of communication of intention to grant

Free format text: ORIGINAL CODE: EPIDOS AGRA

GRAH Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOS IGRA

GRAH Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOS IGRA

GRAH Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOS IGRA

GRAH Despatch of communication of intention to grant a patent

Free format text: ORIGINAL CODE: EPIDOS IGRA

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

ITF It: translation for a ep patent filed
AK Designated contracting states

Kind code of ref document: B1

Designated state(s): BE CH DE ES FI FR GB IT LI NL

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: LI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20001011

Ref country code: FI

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20001011

Ref country code: ES

Free format text: THE PATENT HAS BEEN ANNULLED BY A DECISION OF A NATIONAL AUTHORITY

Effective date: 20001011

Ref country code: CH

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20001011

Ref country code: BE

Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT

Effective date: 20001011

REG Reference to a national code

Ref country code: CH

Ref legal event code: EP

REF Corresponds to:

Ref document number: 69703260

Country of ref document: DE

Date of ref document: 20001116

ET Fr: translation filed
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20010208

Year of fee payment: 5

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: GB

Payment date: 20010219

Year of fee payment: 5

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: DE

Payment date: 20010222

Year of fee payment: 5

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20010226

Year of fee payment: 5

REG Reference to a national code

Ref country code: CH

Ref legal event code: PL

PLBE No opposition filed within time limit

Free format text: ORIGINAL CODE: 0009261

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT

26N No opposition filed
REG Reference to a national code

Ref country code: GB

Ref legal event code: IF02

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: GB

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20020314

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20021001

Ref country code: DE

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20021001

GBPC Gb: european patent ceased through non-payment of renewal fee

Effective date: 20020314

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: FR

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20021129

NLV4 Nl: lapsed or anulled due to non-payment of the annual fee

Effective date: 20021001

REG Reference to a national code

Ref country code: FR

Ref legal event code: ST

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: IT

Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES

Effective date: 20050314