EP0721492A1 - Additifs et compositons de combustibles - Google Patents

Additifs et compositons de combustibles

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Publication number
EP0721492A1
EP0721492A1 EP94924280A EP94924280A EP0721492A1 EP 0721492 A1 EP0721492 A1 EP 0721492A1 EP 94924280 A EP94924280 A EP 94924280A EP 94924280 A EP94924280 A EP 94924280A EP 0721492 A1 EP0721492 A1 EP 0721492A1
Authority
EP
European Patent Office
Prior art keywords
oil
fuel oil
component
carbon atoms
fuel
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
EP94924280A
Other languages
German (de)
English (en)
Other versions
EP0721492B1 (fr
EP0721492B2 (fr
Inventor
Brian William Davies
Allessandro Lombardi
Dhanesh Gordon Goberdhan
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.)
Infineum USA LP
Original Assignee
Exxon Chemical Patents Inc
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
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Application filed by Exxon Chemical Patents Inc filed Critical Exxon Chemical Patents Inc
Priority to EP98202903A priority Critical patent/EP0885948B1/fr
Priority to EP98204020A priority patent/EP0908507A1/fr
Publication of EP0721492A1 publication Critical patent/EP0721492A1/fr
Publication of EP0721492B1 publication Critical patent/EP0721492B1/fr
Application granted granted Critical
Publication of EP0721492B2 publication Critical patent/EP0721492B2/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS 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
    • C10L10/00—Use of additives to fuels or fires for particular purposes
    • C10L10/08—Use of additives to fuels or fires for particular purposes for improving lubricity; for reducing wear
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C—CHEMISTRY; METALLURGY
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    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/143—Organic compounds mixtures of organic macromolecular compounds with organic non-macromolecular compounds
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    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/16—Hydrocarbons
    • C10L1/1625—Hydrocarbons macromolecular compounds
    • C10L1/1633—Hydrocarbons macromolecular compounds homo- or copolymers obtained by reactions only involving carbon-to carbon unsaturated bonds
    • C10L1/1641—Hydrocarbons macromolecular compounds homo- or copolymers obtained by reactions only involving carbon-to carbon unsaturated bonds from compounds containing aliphatic monomers
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    • C10L1/00—Liquid carbonaceous fuels
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    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/1811—Organic compounds containing oxygen peroxides; ozonides
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    • C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
    • C10L1/1822—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
    • C10L1/1824—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy
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    • C10L1/188—Carboxylic acids; metal salts thereof
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    • C10L1/19—Esters ester radical containing compounds; ester ethers; carbonic acid esters
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    • C10L1/19—Esters ester radical containing compounds; ester ethers; carbonic acid esters
    • C10L1/191—Esters ester radical containing compounds; ester ethers; carbonic acid esters of di- or polyhydroxyalcohols
    • C—CHEMISTRY; METALLURGY
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    • C10L1/192—Macromolecular compounds
    • C10L1/195—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS 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
    • C10L1/00—Liquid carbonaceous fuels
    • C10L1/10—Liquid carbonaceous fuels containing additives
    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/192—Macromolecular compounds
    • C10L1/195—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/196—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and a carboxyl group or salts, anhydrides or esters thereof homo- or copolymers of compounds having one or more unsaturated aliphatic radicals each having one carbon bond to carbon double bond, and at least one being terminated by a carboxyl radical or of salts, anhydrides or esters thereof
    • C10L1/1966—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and a carboxyl group or salts, anhydrides or esters thereof homo- or copolymers of compounds having one or more unsaturated aliphatic radicals each having one carbon bond to carbon double bond, and at least one being terminated by a carboxyl radical or of salts, anhydrides or esters thereof poly-carboxylic
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS 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
    • C10L1/00—Liquid carbonaceous fuels
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    • C10L1/14—Organic compounds
    • C10L1/18—Organic compounds containing oxygen
    • C10L1/192—Macromolecular compounds
    • C10L1/195—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/197—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and an acyloxy group of a saturated carboxylic or carbonic acid
    • C10L1/1973—Macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds derived from monomers containing a carbon-to-carbon unsaturated bond and an acyloxy group of a saturated carboxylic or carbonic acid mono-carboxylic
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS 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
    • C10L1/00—Liquid carbonaceous fuels
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    • C10L1/14—Organic compounds
    • C10L1/22—Organic compounds containing nitrogen
    • C10L1/222—Organic 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
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS 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
    • C10L1/00—Liquid carbonaceous fuels
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    • C10L1/14—Organic compounds
    • C10L1/22—Organic compounds containing nitrogen
    • C10L1/222—Organic 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
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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    • C10L1/22—Organic compounds containing nitrogen
    • C10L1/222—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
    • C10L1/224—Amides; Imides carboxylic acid amides, imides
    • C—CHEMISTRY; METALLURGY
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    • C10L1/23—Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites
    • C10L1/231—Organic compounds containing nitrogen containing at least one nitrogen-to-oxygen bond, e.g. nitro-compounds, nitrates, nitrites nitro compounds; nitrates; nitrites
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    • C10L1/238—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds
    • C10L1/2383—Polyamines or polyimines, or derivatives thereof (poly)amines and imines; derivatives thereof (substituted by a macromolecular group containing 30C)
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Definitions

  • This invention relates to the use of additives for improving the cold flow properties of fuel oil, for example distillate petroleum fuel such as middle distillate fuel oil boiling within the range of 110°C to 500°C.
  • fuel oil for example distillate petroleum fuel such as middle distillate fuel oil boiling within the range of 110°C to 500°C.
  • wax may separate out from the fuel and impair the flow properties of the oil.
  • middle distillate fuels contain wax which precipitates at low temperatures to form large waxy crystals which tend to plug the small pore openings of fuel filters. This problem is particularly acute when the fuel is a diesel fuel because the nominal apertures in the fuel filter of diesel engines are typically of diameter between about 5 and 50 microns.
  • Additives are known in the art for overcoming the above problem and are called Flow Improvers.
  • Such additives may act as wax crystal modifiers when blended with waxy mineral oil by modifying the shape and size of crystals of the wax therein and reducing the adhesive forces between the crystals and between the wax and the oil to permit the oil to remain fluid at a lower temperature than in the absence of the additive.
  • additives are described in the art for improving the cold-flow properties of oils, for example in the form of oil-soluble addition products or condensates that may be polymeric or monomeric and as described, for example, in US-A-3,048,479; UK-A-1 ,263,152; US-A-3,961 ,961 ; and EP-A-0,261 ,957.
  • Some of the above additives have been and are used commercially as Cold Flow Improvers.
  • a first aspect of the invention is the use of a co-additive selected from component (A) which comprises one or more of
  • an oil-soluble ashless dispersant/detergent comprising an amine that is acylated with a hydrocarbyl-carboxy acylating agent or that is hydrocarbylated or that is hydrocarboxylated;
  • an oil-soluble lubricity additive comprising an ester of a carboxylic acid and an alcohol wherein the acid has from 2 to 50 carbon atoms and the alcohol has one or more carbon atoms;
  • an oil-soluble petroleum fuel anti-foam comprising a silicon-based composition or a polyamine having at least one primary or secondary amino group, acylated with a carboxylic acylating agent;
  • component (B) which comprises a cold flow improver additive comprising a copolymeric ethylene flow improver, and being to enhance the cold flow properties of the composition.
  • a second aspect of the invention is a process for blending additives with a fuel oil comprising
  • step (iv) adjusting the relative rate of injection of components (B) and (A) and thereby their relative proportions to take account of the results of step (iii) and to provide desired cold flow properties in the fuel oil.
  • the fuel oil is preferably in the form of a flowing stream wherein step (i) takes places at a first station and step (ii) takes place at a second station, though the first and second stations may be co ⁇ terminous and injection be via a common injector.
  • the process can be automated so that a sensor can carry out step (iii), e.g. by measuring the cold filter plugging point (CFPP), and the information fed via a controller to control injection of one or both of components (B) and (A).
  • CFPP cold filter plugging point
  • the invention surprisingly enables less of component (B) to be used to achieve a desired cold flow improvement performance.
  • hydrocarbyl refers to a group having a carbon atom directly attached to the rest of the molecule and having a hydrocarbon or predominantly hydrocarbon character.
  • hydrocarbon groups including aliphatic (e.g. alkyl or alkenyl), alicyclic (e.g. cycloalkyl or cycloalkenyl), aromatic, and alicyclic-substituted aromatic, and aromatic-substituted aliphatic and alicyclic groups.
  • Aliphatic groups are advantageously saturated. These groups may contain non-hydrocarbon substituents provided their presence does not alter the predominantly hydrocarbon character of the group. Examples include keto, halo, hydroxy, nitro, cyano, alkoxy and acyl. If the hydrocarbyl group is substituted, a single (mono) substituent is preferred.
  • substituted hydrocarbyl groups include 2-hydroxyethyl, 3-hydroxypropyl, 4-hydroxybutyl, 2-ketoprop l, ethoxyethyl, and propoxyprop l.
  • the groups may also or alternatively contain atoms other than carbon in a chain or ring otherwise composed of carbon atoms. Suitable hetero atoms include, for example, nitrogen, sulphur, and, preferably, oxygen.
  • ashless dispersants are dispersants for improving the detergency of fuel oils and leave little or no metal-containing residue on combustion. They are described in numerous patent specifications and include the following:
  • hydrocarbyl polycarboxy acylating agents e.g. hydrocarbyl dicarboxylic anhydride
  • alkenyl succinimide polyamines for example where the alkenyl group is polyisobutylene.
  • hydrocarbyl polycarboxy acylating agents e.g. hydrocarbyl dicarboxylic anhydride
  • alkenyl succinimide polyamines for example where the alkenyl group is polyisobutylene.
  • alkenyl group is polyisobutylene
  • hydrocarbyl ether amines such as alkyl ether monoamines, for example where the hydrocarbyl group has from 6 to 26 carbon atoms (e.g. 8 or
  • the amine may, for example have 2 to 8 carbon atoms. Examples are described in US-A-4,319,987. Other examples are alkoxylated amines such as described in US-A-4,409,000.
  • the acid from which the ester is derived may be a mono or polycarboxylic acid such as aliphatic, saturated or unsaturated, straight or branched chain, mono and dicarboxylic acids being preferred.
  • the acid may be generalised in the formula
  • R'(COOH) x where x represents an integer and is 1 or more such as 1 to 4, and R' represents a hydrocarbyl group having from 2 to 50 carbon atoms and which is mono or polyvalent corresponding to the value of x, the -COOH groups, when more than one is present, optionally being substituent on different carbon atoms from one another.
  • 'Hydrocarbyl means a group containing carbon and hydrogen which group is connected to the rest of the molecule via a carbon atom. It may be straight or branched chain which chain may be interrupted by one or more hereto atoms such as O, S, N or P, may be saturated or unsaturated, may be aliphatic or alicyclic or aromatic including heterocyclic, or may be substituted or unsubstituted.
  • the hydrocarbyl group is an alkyl group or an alkenyl group having 10 (e.g. 12) to 30 carbon atoms, i.e. the acid is saturated or unsaturated.
  • the alkenyl group may have one or more double bonds, such as 1 , 2 or 3.
  • saturated carboxylic acids are those with 10 to 22 carbon atoms such as oleic, elaidic, palmitoleic, petroselic, conoleic, eleostrearic, linoleic, linolenic, eicosanoic, galoliec, erucic and hypogeic acids.
  • the acid is polycarboxylic, having for example from 2 to 4 carboxy groups
  • the hydrocarbyl group is preferably a substituted or unsubstituted polymethylene.
  • the alcohol from which the ester is derived may be a mono or polyhydroxy alcohol such as a trihydroxy alcohol.
  • the alcohol may be generalised in the formula
  • y represents an integer and is 1 or more and R-- represents a hydrocarbyl group having 1 or more carbon atoms such as up to 10 carbon atoms, and which is mono or polyvalent corresponding to the value of y, the -OH groups, when more than one is present, optionally being substituent on different carbon atoms from one another.
  • the hydrocarbyl group is preferably an alkyl group or a substituted or unsubstituted polymethylene group.
  • rnonohydhc alcohols are lower alkyl alcohols having from 1 to 6 carbon atoms such as methyl, ethyl, propyl and butyl alcohols.
  • polyhydric alcohols are aliphatic, saturated or unsaturated, straight chain or branched alcohols having 2 to 10, preferably 2 to 6, more preferably 2 to 4, hydroxy groups, and having 2 to 90, preferably 2 to 30, more preferably 2 to 12, most preferably 2 to 5, carbon atoms in the molecule.
  • the polyhydric alcohol may be a glycol or diol, or a t hydric alcohol such as glycerol.
  • the esters may be used alone or as mixtures of one or more esters and may be composed only of carbon, hydrogen and oxygen.
  • the ester has a molecular weight of 200 or greater, or has at least 10 carbon atoms, or has both.
  • esters examples include lower alkyl esters, such as methyl esters, of the above exemplified saturated or unsaturated monocarboxylic acids. Such esters may, for example, be obtained by saponificaton and esterification of natural fats and oils of plant or animal origin or by their transesterification with lower aliphatic alcohols.
  • esters of polyhydric alcohols that may be used are those where all of the hydroxy groups are esterified, those where not all of the hydroxy groups are esterified, and mixtures thereof.
  • Specific examples are esters prepared from trihydric alcohols and one or more of the above-mentioned saturated or unsaturated carboxylic acids, such as glycerol monoesters and glycerol diesters, e.g. glycerol monooleate, glycerol dioleate and glycerol monostearate.
  • Such polyhydric esters may be prepared by esterification as described in the art and/or may be commercially available.
  • the ester may have one or more free hydroxy groups.
  • cetane improvers are organic nitrates, such as nitrate esters containing aliphatic or cyclo-aliphatic groups with up to 30 carbon atoms, preferably saturated groups, and preferably with up to 12 carbon atoms.
  • nitrates examples include methyl, ethyl, propyl, isopropyl, butyl, amyl, hexyl, heptyl, octyl, iso-octyl, 2-ethylhexyl, nonyl, decyl, allyl, cyclo-pentyl, cyclohexyl, methycyclohexyl, cyclodecyl, 2-ethoxyethyl, and 2-(2- ethoxylethoxy)ethyl nitrates.
  • Other examples are fuel soluble peroxides, hydroperoxides and peroxy esters.
  • Examples of anti-foams include siloxane-polyoxyalkylene copolymers, for example those described in U.S. Patent No. 3 233 986, the disclosure of which is incorporated by reference herein, which comprise at least one siloxane block containing at least two siloxane groups of the formula R2SiOo.5(4- ) wherein R represents a halogen atom or an optionally halogenated hydrocarbon group and b represents from 1 to 3, and at least one polyoxylalkylene block containing at least two oxyalkylene groups.
  • the alkylene groups have 2 or 3 carbon atoms, and usually both ethylenoxy and propyleneoxy groups are present.
  • the copolymer is a polymethylsiloxane-polyoxylalkylene copolymer, preferably of the general formula
  • Z represents hydrocarbyl, OC(hydrocarbyl) or, preferably, hydrogen, and in which the absolute values of m and n, and their ratios, and the values of p, x, and y, and their ratios, may vary widely but total values advantageously give a weight average molecular weight in the range of from 600 to 25000.
  • the ratio of m:n is advantageously in the range of from 10:1 to 1 :20, or the value of n may be zero, and the ratio of x:y is advantageously in the range of from 1 :100 to 100:1 , preferably 20:80 to 100:1 , or one of x or y, but not both, may be zero.
  • Preferred foam inhibitors are those sold under the trade mark TEGOPREN by Th. Goldschmidt AG.
  • the foam inhibitor is present in the fuel in a proportion in the range of from 0.0001 to 0.2% , preferably from 0.005 to 0.02%, by weight.
  • Other anti-foams may be non-silicon containing such as those made by acylating polyamines as described in WO 94/06894. COMPONENT (B)
  • Ethylene copolymer flow improvers e.g. ethylene/unsaturated ester copolymer flow improvers have a polymethylene backbone divided into segments by oxyhydrocarbon side chains.
  • the copolymer may comprise an ethylene copolymer having, in addition to units derived from ethylene, units of the formula
  • R 6 represents hydrogen or a methyl group
  • R5 represents a -OOCR 8 or -COOR 8 group wherein R 8 represents hydrogen or a C-] to C28. preferably C1 to C9, straight or branched chain alkyl group, provided that R 8 does not represent hydrogen when R 5 represents -COOR 8 ; and R 7 is hydrogen or -COOR 8 .
  • These may comprise a copolymer of ethylene with an ethylenically unsaturated ester, or derivatives thereof.
  • An example is a copolymer of ethylene with an ester of an unsaturated carboxylic acid, but the ester is preferably one of an unsaturated alcohol with a saturated carboxylic acid.
  • An ethylene-vinyl ester copolymer is advantageous; an ethylene-vinyl acetate, ethylene vinyl propionate, ethylene-vinyl hexanoate, or ethylene-vinyl octanoate copolymer is preferred.
  • the copolymers contain from 1 to 25, e.g.
  • the copolymers may be derived from additional comonomers, e.g. they may be terpolymers or tetrapolymers or higher polymers, for example where the additional comonomer is isobutylene or diisobutylene.
  • the copolymers may be made by direct polymerisation of comonomers. Such copolymers may also be made by transesterification, or by hydrolysis and re- estehfication, of an ethylene unsaturated ester copolymer to give a different ethylene unsaturated ester copolymer.
  • ethylene vinyl hexanoate and ethylene vinyl octanoate copolymers may be made in this way, e.g. from an ethylene vinyl acetate copolymer.
  • Component (B) may be used with co-components such as one or more of the following:
  • Comb polymers are discussed in "Comb-Like Polymers. Structure and Properties", N. A. Plate and V. P. Shibaev, J. Poly. Sci. Macromolecular Revs., 8, p 117 to 253 (1974).
  • comb polymers have one or more long chain branches such as hydrocarbyl branches, such as oxyhydrocarbyl branches, having from 10 to 30 carbon atoms, pendant from a polymer backbone, said branch or branches being bonded directly or indirectly to the backbone.
  • long chain branches such as hydrocarbyl branches, such as oxyhydrocarbyl branches, having from 10 to 30 carbon atoms, pendant from a polymer backbone, said branch or branches being bonded directly or indirectly to the backbone.
  • indirect bonding include bonding via interposed atoms or groups, which bonding can include covalent and/or electrovalent bonding such as in a salt.
  • the comb polymer is a homopolymer having, or a copolymer at least 25 and preferably at least 40, more preferably at least 50, molar per cent of the units of which have, side chains containing at least 6, and preferably at least 10, atoms, selected from for example carbon, nitrogen and oxygen, in a linear chain.
  • J H, R 12 , R 12 COOR 11 , or an aryl or heterocyclic group
  • K H, COOR 12 , OCOR 12 , OR 12 or COOH
  • L H, R 12 COOR 12 , OCOR 12 or aryl
  • R 1 C10 hydrocarbyl
  • R 12 - Ci hydrocarbyl and m and n represent mole ratios, their sum being 1 and m being finite and being up to and including 1 and n being from zero to less than 1 , preferably m being within the range of from 1.0 to 0.4, n being in the range of from 0 to 0.6.
  • R11 advantageously represents a hydrocarbyl group with from 10 to 30 carbon atoms
  • R 12 advantageously represents a hydrocarbyl group with from 1 to 30 carbon atoms.
  • the comb polymer may contain units derived from other monomers if desired or required. It is within the scope of the invention to include two or more different comb copolymers.
  • These comb polymers may be copolymers of maleic anhydride or fumaric acid and another ethylenically unsaturated monomer, e.g. an ⁇ -olefin or an unsaturated ester, for example, vinyl acetate. It is preferred but not essential that equimolar amounts of the comonomers be used although molar proportions in the range of 2 to 1 and 1 to 2 are suitable.
  • olefins that may be copolymerized with e.g. maleic anhydride, include 1-decene, 1-dodecene, 1- tetradecene, 1 -hexadecene, and 1 -octadecene.
  • the copolymer may be esterified by any suitable technique and although preferred it is not essential that the maleic anhydride or fumaric acid be at least 50% esterified.
  • examples of alcohols which may be used include n-decan-1-ol, n-dodecan-1-ol, n-tetradecan-1-ol, n-hexadecan-1-ol, and n-octadecan-1-ol.
  • the alcohols may also include up to one methyl branch per chain, for example, 1-methylpentadecan-1-ol, 2-methyltridecan-1-ol.
  • the alcohol may be a mixture of normal and single methyl branched alcohols.
  • R 12 refers to the average number of carbon atoms in the alkyl group; if alcohols that contain a branch at the 1 or 2 positions are used R 12 refers to the straight chain backbone segment of the alcohol.
  • These comb polymers may especially be fumarate or itaconate polymers and copolymers such as for example those described in European Patent Applications 153 176, 153 177 and 225 688, and WO 91/16407.
  • Particularly preferred fumarate comb polymers are copolymers of alkyl fumarates and vinyl acetate, in which the alkyl groups have from 12 to 20 carbon atoms, more especially polymers in which the alkyl groups have 14 carbon atoms or in which the alkyl groups are a mixture of C14/C16 alkyl groups, made, for example, by solution copolymerizing an equimolar mixture of fumaric acid and vinyl acetate and reacting the resulting copolymer with the alcohol or mixture of alcohols, which are preferably straight chain alcohols.
  • the mixture it is advantageously a 1 :1 by weight mixture of normal C14 and C16 alcohols.
  • mixtures of the C14 ester with the mixed C14/C16 ester may advantageously be used.
  • the ratio of C14 to C14/C16 is advantageously in the range of from 1 :1 to 4:1 , preferably 2:1 to 7:2, and most preferably about 3:1 , by weight.
  • the particularly preferred fumarate comb polymers may, for example, have a number average molecular weight in the range of 1 ,000 to 100,000, preferably 1 ,000 to 30,000, as measured by Vapour Phase Osmometry (VPO).
  • comb polymers are the polymers and copolymers of ⁇ -olefins and esterified copolymers of styrene and maleic anhydride, and esterified copolymers of styrene and fumaric acid; mixtures of two or more comb polymers may be used in accordance with the invention and, as indicated above, such use may be advantageous.
  • comb polymers are hydrocarbon polymers such as copolymers of ethylene and at least one ⁇ -olefin, preferably the ⁇ -olefin having at most 20 carbon atoms, examples being n-decene-1 and n-dodecene-1.
  • the number average molecular weight of such a copolymer is at least 30,000.
  • the hydrocarbon copolymers may be prepared by methods known in the art, for example using a Ziegler type catalyst.
  • Such compounds comprise a compound in which at least one substantially linear alkyl group having 10 to 30 carbon atoms is connected to a non-polymeric organic residue to provide at least one linear chain of atoms that includes the carbon atoms of said alkyl groups and one or more non-terminal oxygen atoms.
  • substantially linear is meant that the alkyl group is preferably straight chain, but that essentially straight chain alkyl groups having a small degree of branching such as in the form of a single methyl group may be used.
  • the compound has a least two of said alkyl groups when the linear chain may include the carbon atoms of more than one of said alkyl groups.
  • the compound has at least three of said alkyl groups, there may be more than one of such linear chains, which chains may overlap.
  • the linear chain or chains may provide part of a linking group between any two such alkyl groups in the compound.
  • the oxygen atom or atoms are preferably directly interposed between carbon atoms in the chain and may, for example, be provided in the form of a mono- or poly-oxyalkylene group, said oxyalkylene group preferably having 2 to 4 carbon atoms, examples being oxyethylene and oxypropylene.
  • chain or chains include carbon and oxygen atoms. They may also include other hetero-atoms such as nitrogen atoms.
  • the compound may be an ester where the alkyl groups are connected to the remainder of the compound as -O-CO n alkyl, or -CO-O n alkyl groups, in the former the alkyl groups being derived from an acid and the remainder of the compound being derived from a polyhydric alcohol and in the latter the alkyl groups being derived from an alcohol and the remainder of the compound being derived from a polycarboxylic acid.
  • the compound may be an ester where the alkyl groups are connected to the remainder of the compound as — O — n — alkyl groups.
  • the compound may be both an ester and an ether or it may contain different ester groups.
  • Examples include polyoxyalkylene esters, ethers, ester/ethers and mixtures thereof, particularly those containing at least one, preferably at least two, C « ⁇ o to C30 linear alkyl groups and a polyoxyalkylene glycol group of molecular weight up to 5,000, preferably 200 to 5,000, the alkylene group in said polyoxyalkylene glycol containing from 1 to 4 carbon atoms, as described in EP-A-61 895 and in U.S. Patent No. 4,491 ,455.
  • the preferred esters, ethers or ester/ethers which may be used may be structurally depicted by the formula
  • R 23 OBOR 24 where R 23 and R 24 are the same or different and may be
  • n-alkyl-OCO-(CH 2 ) n CO- n being, for example, 1 to 34, the alkyl group being linear and containing from 10 to 30 carbon atoms
  • B representing the polyalkylene segment of the glycol in which the alkylene group has from 1 to 4 carbon atoms, for example, polyoxymethylene, polyoxyethylene or polyoxytrimethylene moiety which is substantially linear; some degree of branching with lower alkyl side chains (such as in polyoxypropylene glycol) may be tolerated but it is preferred that the glycol should be substantially linear.
  • B may also contain nitrogen.
  • Suitable glycols generally are substantially linear polyethylene glycols (PEG) and polypropylene glycols (PPG) having a molecular weight of about 100 to 5,000, preferably about 200 to 2,000.
  • Esters are preferred and fatty acids containing from 10 to 30 carbon atoms are useful for reacting with the glycols to form the ester additives, it being preferred to use C-J S to C24 fatty acid, especially behenic acid.
  • the esters may also be prepared by esterifying polyethoxylated fatty acids or polyethoxylated alcohols.
  • Polyoxyalkylene diesters, diethers, ether/esters and mixtures thereof are suitable as additives, diesters being preferred when the petroleum based component is a narrow boiling distillate, when minor amounts of monoethers and monoesters (which are often formed in the manufacturing process) may also be present. It is important for active performance that a major amount of the dialkyl compound is present.
  • stearic or behenic diesters of polyethylene glycol, polypropylene glycol or polyethylene/polypropylene glycol mixtures are preferred.
  • v and w represent mole ratios, v being within the range 1.0 to 0.0, w being within the range 0.0 to 1.0.
  • These polymers may be made directly from ethylenically unsaturated monomers or indirectly by hydrogenating the polymer made from monomers such as isoprene and butadiene.
  • Preferred hydrocarbon polymers are copolymers of ethylene and at least one ⁇ - olefin, having a number average molecular weight of at least 30,000.
  • the ⁇ -olefin has at most 20 carbon atoms.
  • Examples of such olefins are propylene, 1 -butene, isobutene, n-octene-1 , isooctene-1 , n-decene-1 , and n-dodecene-1.
  • the copolymer may also comprise small amounts, e.g. up to 10% by weight of other copolymerizable monomers, for example olefins other than ⁇ - olefins, and non-conjugated dienes.
  • the preferred copolymer is an ethylene- propylene copolymer. It is within the scope of the invention to include two or more different ethylene- ⁇ -olefin copolymers of this type.
  • the number average molecular weight of the ethylene- ⁇ -olefin copolymer is, as indicated above, at least 30,000, as measured by gel permeation chromatography (GPC) relative to polystyrene standards, advantageously at least 60,000 and preferably at least 80,000. Functionally no upper limit arises but difficulties of mixing result from increased viscosity at molecular weights above about 150,000, and preferred molecular weight ranges are from 60,000 and 80,000 to 120,000.
  • the copolymer has a molar ethylene content between 50 and 85 per cent. More advantageously, the ethylene content is within the range of from 57 to 80%, and preferably it is in the range from 58 to 73%; more preferably from 62 to 71 %, and most preferably 65 to 70%.
  • Preferred ethylene- ⁇ -olefin copolymers are ethylene-propylene copolymers with a molar ethylene content of from 62 to 71 % and a number average molecular weight in the range 60,000 to 120,000, especially preferred copolymers are ethylene-propylene copolymers with an ethylene content of from 62 to 71% and a molecular weight from 80,000 to 100,000.
  • the copolymers may be prepared by any of the methods known in the art, for example using a Ziegler type catalyst.
  • the polymers are substantially amorphous, since highly crystalline polymers are relatively insoluble in fuel oil at low temperatures.
  • the additive composition may also comprise a further ethylene- ⁇ -olefin copolymer, advantageously with a number average molecular weight of at most 7500, advantageously from 1 ,000 to 6,000, and preferably from 2,000 to 5,000, as measured by vapour phase osmometry.
  • ⁇ -olefins are as given above, or styrene, with propylene again being preferred.
  • the ethylene content is from 60 to 77 molar per cent although for ethylene-propylene copolymers up to 86 molar per cent by weight ethylene may be employed with advantage.
  • hydrocarbon polymers examples are described in WO-A-9 111 488.
  • the oil-soluble polar nitrogen compound is either ionic or non-ionic and is capable of acting as a wax crystal growth inhibitor in fuels.
  • Ester/amides may be used containing 30 to 300, preferably 50 to 150 total carbon atoms. These nitrogen compounds are described in US Patent 4 211 534. Suitable amines are usually long chain C12-C40 primary, secondary, tertiary or quaternary amines or mixtures thereof but shorter chain amines may be used provided the resulting nitrogen compound is oil soluble and therefore normally contains about 30 to 300 total carbon atoms.
  • the nitrogen compound preferably contains at least one straight chain Cs to C40, preferably C14 to C24 . alkyl segment.
  • Suitable amines include primary, secondary, tertiary or quaternary, but preferably are secondary. Tertiary and quaternary amines can only form amine salts. Examples of amines include tetradecyl amine, cocoamine, and hydrogenated tallow amine. Examples of secondary amines include dioctacedyl amine and methyl-behenyl amine. Amine mixtures are also suitable such as those derived from natural materials.
  • a preferred amine is a secondary hydrogenated tallow amine of the formula HNR 1 R 2 wherein R and R 2 are alkyl groups derived from hydrogenated tallow fat composed of approximately 4% C14, 31 % Ci6, 59% C ⁇ -
  • suitable carboxylic acids and their anhydrides for preparing the nitrogen compounds include cyclohexane 1 ,2 dicarboxylic acid, cyclohexene 1 ,2 dicarboxylic acid, cyclopentane 1 ,2 dicarboxylic acid and naphthalene dicarboxylic acid, and 1 ,4-dicarboxylic acids including dialkyl spirobislactone. Generally, these acids have about 5-13 carbon atoms in the cyclic moiety.
  • Preferred acids useful in the present invention are benzene dicarboxylic acids such as phthalic acid, isophthalic acid, and terephthalic acid. Phthalic acid or its anhydride is particularly preferred.
  • the particularly preferred compound is the amide-amine salt formed by reacting 1 molar portion of phthalic anhydride with 2 molar portions of dihydrogenated tallow amine.
  • Another preferred compound is the diamide formed by dehydrating this amide-amine salt.
  • Other examples are long chain alkyl or alkylene substituted dicarboxylic acid derivatives such as amine salts of monoamides of substituted succinic acids, examples of which are known in the art and described in US-A-4 147 520, for example. Suitable amines may be those described above.
  • A is an aliphatic hydrocarbyl group that is optionally interrupted by one or more hetero atoms and that is straight chain or branched
  • R 1 and R 2 are the same or different and each is independently a hydrocarbyl group containing 9 to 40 carbon atoms optionally interrupted by one or more hetero atoms, the substituents being the same or different and the compound optionally being in the form of a salt thereof.
  • A has from 1 to 20 carbon atoms and is preferably a methylene or polymethylene group.
  • hydrocarbyl refers to a group having a carbon atom directly attached to the rest of the molecule and having a hydrocarbon or predominantly hydrocarbon character.
  • hydrocarbon groups including aliphatic (e.g. alkyl or alkenyl), alicyclic (e.g. cycloalkyl or cycloalkenyl), aromatic, and alicyclic-substituted aromatic, and aromatic-substituted aliphatic and alicyclic groups.
  • Aliphatic groups are advantageously saturated. These groups may contain non-hydrocarbon substituents provided their presence does not alter the
  • hydrocarbyl group is substituted, a single (mono) substituent is preferred.
  • substituted hydrocarbyl groups examples include 2-hydroxyethyl, 3-hydroxypropyl, 4-hydroxy butyl, 2-ketopropyl, ethoxyethyl, and propoxypropyl.
  • the groups may also or alternatively contain atoms other than carbon in a chain or ring otherwise composed of carbon atoms. Suitable hetero atoms include, for example, nitrogen, sulphur, and, preferably, oxygen.
  • the cyclic ring system may include homocyclic, heterocyclic, or fused polycyclic assemblies, or a system where two or more such cyclic assemblies are joined to one another and in which the cyclic assemblies may be the same or different.
  • the substituents of the general formula (I) may be on the same or different assemblies, preferably on the same assembly.
  • the or each cyclic assembly is aromatic, more preferably a benzene ring.
  • the cyclic ring system is a single benzene ring when it is preferred that the substituents are in the ortho or meta positions, which benzene ring may be optionally further substituted.
  • the ring atoms in the cyclic assembly or assemblies are preferably carbon atoms but may for example include one or more ring N, S or O atom, in which case or cases the compound is a heterocyclic compound.
  • polycyclic assemblies examples include
  • heterocyclic compounds such as quinoline, indole, 2:3 dihydroindole, benzofuran, coumarin, isocoumarin, benzothiophen, carbazole and thiodiphenylamine;
  • non-aromatic or partially saturated ring systems such as decalin (i.e. decahydronaphthalene), ⁇ -pinene, cardinene, and bomylene; and
  • each hydrocarbyl group constituting R 1 and R 2 in the invention may for example be an alkyl or alkylene group or a mono- or poly-alkoxyalkyl group.
  • each hydrocarbyl group is a straight chain alkyl group.
  • the number of carbon atoms in each hydrocarbyl group is preferably 16 to 40, more preferably 16 to 24.
  • the cyclic system is substituted with only two substituents of the general formula (I) and that A is a methylene group.
  • salts of the chemical compounds are the acetate and the hydrochloride.
  • the compounds may conveniently be made by reducing the corresponding amide which may be made by reacting a secondary amine with the appropriate acid chloride;
  • polymers such as described in GB-A-2,121 ,807, FR-A-2,592,387 and DE-A-3,941 ,561 ; and also esters of telemer acid and alkanoloamines such as described in US-A-4,639,256; and the reaction product of an amine containing a branched carboxylic acid ester, an episode and a mono- carboxylic acid polyester such as described in US-A4,631 ,071.
  • the fuel oil is suitably a middle distillate fuel oil.
  • distillate fuel oils generally boil within the range of about 110°C to about 500°C, e.g. 150° to about 400°C.
  • the fuel oil can comprise atmospheric distillate or vacuum distillate, or cracked gas oil or a blend in any proportion of straight run and thermally and/or catalytically cracked distillates.
  • the most common petroleum distillate fuels are kerosene, jet fuel, diesel fuels, heating oil and heavy fuel oils.
  • the heating oil may be a straight atmospheric distillate, or it may contain minor amounts, e.g. up to 35 wt%, of vacuum gas oil or cracked gas oils or of both.
  • the fuel oil may be animal, vegetable or mineral oil and may also be synthetic. It may also contain additives other than those mentioned hereinbefore.
  • the concentration of the additive combination in the oil may for example be in the range of 1 to 5,000 ppm of additive (active ingredient) by weight per weight of fuel, such as 10 to 2000 ppm (active ingredient) by weight per weight of fuel, preferably 25 to 500 ppm, more preferably 100 to 200 ppm.
  • the additive should be soluble in the oil to the extent of at least 1000 ppm by weight of oil at ambient temperature. However, at least some of the additive may come out of solution near the cloud point of the oil in order to modify the wax crystals that form.
  • Concentrates are convenient as a means for incorporating the additive into bulk oil such as distillate fuel, which incorporation may be done by methods known in the art.
  • the concentrates may also contain other additives as required and preferably contain from 3 to 75 wt %, more preferably 3 to 60 wt %, most preferably 10 to 50 wt % of the additives preferably in solution in oil.
  • carrier liquid are organic solvents including hydrocarbon solvents, for example petroleum fractions such as naphtha, kerosene and heater oil; aromatic hydrocarbon containing aromatic fractions (e.g. Solvesso (trade name)); and paraffinic hydrocarbons such as hexane, pentane and isoparaffins, and includes mixtures of the above.
  • the carrier liquid must, of course, be selected having regard to its compatibility with the additive and with the fuel.
  • the additives of the invention may be incorporated into bulk oil by other methods such as those known in the art. If others are required, they may be incorporated into the bulk oil at the same time as the additives of the invention or at a different time.
  • other additives include antioxidants, corrosion inhibitors, dehazers, metal deactivators, cosolvents, package compatibilisers, reodorants, antistatic additives (conductivity improvers), biocides, dyes, smoke reducers, catalyst life enhancers, power boosters, additives for fuel economy, demulsifiers, and spray modifiers.
  • B1 an ethylene-vinyl acetate copolymer of number average molecular weight 3,300 as measured by Gel Permeation Chromatography (GPC) and containing about 36% by weight of vinyl acetate.
  • B2 an ethylene-vinyl acetate copolymer of number average molecular weight 5,000 as measured by GPC and containing about 13.5% by weight of vinyl acetate.
  • B3 a mixture of additives B1 and B2 in the weight:weight ratio (B1 :B2) of 3:1.
  • A1 a commercial mixture of polyethylene amines which includes penta ethylene hexamine [NH 2 (CH2)2NH(CH2)2NH(CH2)2NH(CH2)2NH 2 ] and tetraethylene pentamine that has been acylated with a polyisobutylene (molecular weight 950) substituted succinic anhydride to produce a polyisobutylene succinic anhydride-polyamine product.
  • a polyisobutylene molecular weight 950
  • A2 a macrocyclic product obtained by reacting a polyisobutylene (molecular weight 950) substituted succinic anhydride with a polyamine of the formula NH2(CH2)3NH(CH2)2NH(CH2)3NH2 to give an acylated polyamine which is then cyclised as described in EP-A-525,052.
  • A3 an ether amine of the formula R-0-(CH2)3NH2 where R represents one of more iso-C-io alkyl groups, as described in US-A-4,319,987.
  • A4 an octyl nitrate cetane improver as known in the art and as commercially available.
  • A5 an ester obtained by reacting dilinoleic acid (a C36 dimer acid) with ethylene glycol and neutralising acid groups with methanol, as described in US-A-3,287,273.
  • A6 ethoxylated cocoamine, sold commercially as ARMAK 1282.
  • A7 the product formed by reacting one mole of NH2(C2H4)NH(C2H4)OH with slightly in excess of two moles of a mixture of two linear alkanoic acids having 12 and 14 carbon atoms respectively, as described in WO 94/06894.
  • N,N-dialkylammonium salt of 2-N 1 ,N 1 -dialkyl-amido benzoate being the reaction product of reacting one mole of phthalic anhydride with two moles of dihydrogenated tallow amine to form a half amide/half amine salt.
  • CP Cloud Point measured according to IP 219/82
  • CFPP Cold Filter Plugging Point and SFPP is Simulated Filter Plugging
  • Additives were dissolved in the fuels and the following tests performed on fuel treated with additives to measure the following in order to assess the effectiveness of the additives tested as filterability improvers in distillate fuels.
  • the test was carried out by the procedure substantially as described in EP-A-0,403,097 and is a variation of the CFPP test.
  • a sample of the oil to be tested (40 ml) is cooled in a bath which is maintained at about -34°C to give non-linear cooling at about 1 °C/min.
  • the cooled oil tested for its ability to flow through a fine screen in a prescribed time period using a test device which is a pipette to whose lower end is attached an inverted funnel which is positioned below the surface of the oil to be tested. Stretched across the mouth of the funnel is a 350 mesh screen having an area defined by a 12 millimetre diameter.
  • the periodic tests are each initiated by applying a vacuum to the upper end of the pipette whereby oil is drawn through the screen up into the pipette to a mark indicating 20 ml of oil. After each successful passage, the oil is returned immediately to the CFPP tube. The test is repeated with each one degree drop in temperature until the oil fails to fill the pipette within 60 seconds, the temperature at which failure occurs being reported as the CFPP temperature.
  • ⁇ SFPP and ⁇ CFPP represent the difference between the SFPP (or CFPP) of the base ⁇ uel and that of the treated fuel
  • the additive combinations of the invention may also be effective in reducing the tendency of wax in the fuel to settle (i.e. they may be wax anti-settling additives) and may exhibit activity in slow cooling tests such as the Extended Programmed Cooling Test (XPCT) which is known in the art.
  • XPCT Extended Programmed Cooling Test
  • Components BX and BY were used having the following formulations respectively: BX: B2 (56 ppm) B1 (169 ppm) 7 (75 ppm) C (75 ppm)
  • BY B2 (50 ppm) 3 (100 ppm) 6 (100 ppm) C (100 ppm) 5 (200 ppm)
  • the concentrations of the constituents of Components BX and BY in the fuels in the tests to be described hereinafter are given in parentheses as weight per cent of fuel.
  • the constituents, identified by reference numbers 3 and 5 to 7 above, are as follows (additional to constituents already defined herein)
  • an itaconate polymer of number average molecular weight about 4000 as measured by GPC prepared by polymerising a monomer in cyclohexane solvent using a free radical catalyst, the monomer containing linear alkyl groups of 18 carbon atoms.
  • a polyaminated polyisobutylene succinic anhydride detergent 200 ppm
  • an octyl nitrate cetane improver 240 ppm
  • an ethoxylated nonyl phenol antirust 20 ppm
  • a silicon-containing anti-foam 12.5 ppm
  • a reodorant 80 ppm
  • isodecanol 47.5 ppm
  • Solidso 150 (385 ppm) - an aromatic diluent a first demulsifier (5 ppm) a second demulsifier (10 ppm)
  • concentrations of the constituents of Component AY in the fuels in the tests to be described hereinafter are given in parentheses as weight per weight of fuel.
  • SFPP diff. is the difference between the SFPP obtained when Component BX (or BY) alone was used and that obtained when Component BX (or BY) and Component AY were used together.
  • the results show that Component AY enhanced SFPP in three out of four cases.

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  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

Additifs de dispersion, d'augmentation du pouvoir lubrifiant, d'amélioration du cétane et/ou anti-mousse, utilisés conjointement avec des additifs d'amélioration de l'écoulement à base d'éthylène copolymère, et destinés à améliorer les propriétés d'écoulement à froid des mazouts.
EP94924280A 1993-07-22 1994-07-22 Additifs et compositons de combustibles Expired - Lifetime EP0721492B2 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
EP98202903A EP0885948B1 (fr) 1993-07-22 1994-07-22 Utilisation de compositions d'additifs dans un combustible
EP98204020A EP0908507A1 (fr) 1993-07-22 1994-07-22 Additifs et compositions de combustible

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB939315205A GB9315205D0 (en) 1993-07-22 1993-07-22 Additives and fuel compositions
GB9315205 1993-07-22
PCT/EP1994/002432 WO1995003377A1 (fr) 1993-07-22 1994-07-22 Additifs et compositons de combustibles

Related Child Applications (2)

Application Number Title Priority Date Filing Date
EP98204020A Division EP0908507A1 (fr) 1993-07-22 1994-07-22 Additifs et compositions de combustible
EP98202903A Division EP0885948B1 (fr) 1993-07-22 1994-07-22 Utilisation de compositions d'additifs dans un combustible

Publications (3)

Publication Number Publication Date
EP0721492A1 true EP0721492A1 (fr) 1996-07-17
EP0721492B1 EP0721492B1 (fr) 1999-09-15
EP0721492B2 EP0721492B2 (fr) 2002-06-19

Family

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Family Applications (3)

Application Number Title Priority Date Filing Date
EP94924280A Expired - Lifetime EP0721492B2 (fr) 1993-07-22 1994-07-22 Additifs et compositons de combustibles
EP98202903A Revoked EP0885948B1 (fr) 1993-07-22 1994-07-22 Utilisation de compositions d'additifs dans un combustible
EP98204020A Withdrawn EP0908507A1 (fr) 1993-07-22 1994-07-22 Additifs et compositions de combustible

Family Applications After (2)

Application Number Title Priority Date Filing Date
EP98202903A Revoked EP0885948B1 (fr) 1993-07-22 1994-07-22 Utilisation de compositions d'additifs dans un combustible
EP98204020A Withdrawn EP0908507A1 (fr) 1993-07-22 1994-07-22 Additifs et compositions de combustible

Country Status (8)

Country Link
EP (3) EP0721492B2 (fr)
JP (1) JPH09503530A (fr)
KR (1) KR100325574B1 (fr)
CA (1) CA2167672C (fr)
DE (2) DE69434213T2 (fr)
GB (1) GB9315205D0 (fr)
NO (1) NO321605B1 (fr)
WO (1) WO1995003377A1 (fr)

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US7935508B2 (en) 2005-01-19 2011-05-03 Cognis Ip Management Gmbh Production and use of monoglycerides
US8338344B2 (en) 2006-11-17 2012-12-25 Basf Aktiengesellschaft Cold flow improver
US8642521B2 (en) 2003-12-04 2014-02-04 Basf Se Fuel oil compositions with improved cold flow properties

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Publication number Priority date Publication date Assignee Title
US8642521B2 (en) 2003-12-04 2014-02-04 Basf Se Fuel oil compositions with improved cold flow properties
US9605227B2 (en) 2003-12-04 2017-03-28 Basf Se Fuel oil compositions with improved cold flow properties
US10047314B2 (en) 2003-12-04 2018-08-14 Basf Se Fuel oil compositions with improved cold flow properties
US10526558B2 (en) 2003-12-04 2020-01-07 Basf Se Fuel oil compositions with improved cold flow properties
US7935508B2 (en) 2005-01-19 2011-05-03 Cognis Ip Management Gmbh Production and use of monoglycerides
US8338344B2 (en) 2006-11-17 2012-12-25 Basf Aktiengesellschaft Cold flow improver
WO2011001352A1 (fr) 2009-07-03 2011-01-06 Total Raffinage Marketing Terpolymere ethylene/acetate de vinyle/esters insatures comme additif ameliorant la tenue a froid des hydrocarbures liquides comme les distillats moyens et les carburants ou combustibles

Also Published As

Publication number Publication date
DE69420736T3 (de) 2002-11-07
EP0721492B1 (fr) 1999-09-15
DE69434213D1 (de) 2005-02-03
DE69420736D1 (de) 1999-10-21
KR100325574B1 (ko) 2002-07-03
NO960254L (no) 1996-03-15
GB9315205D0 (en) 1993-09-08
KR960704015A (ko) 1996-08-31
DE69434213T2 (de) 2006-01-26
NO960254D0 (no) 1996-01-22
JPH09503530A (ja) 1997-04-08
EP0721492B2 (fr) 2002-06-19
EP0885948A2 (fr) 1998-12-23
EP0885948B1 (fr) 2004-12-29
CA2167672A1 (fr) 1995-02-02
NO321605B1 (no) 2006-06-12
WO1995003377A1 (fr) 1995-02-02
EP0908507A1 (fr) 1999-04-14
EP0885948A3 (fr) 1999-01-27
CA2167672C (fr) 2005-06-21
DE69420736T2 (de) 2000-03-09

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