EP0938535B1 - Detergent and anti-corrosive additive for fuels and fuel composition - Google Patents

Detergent and anti-corrosive additive for fuels and fuel composition Download PDF

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Publication number
EP0938535B1
EP0938535B1 EP97919109A EP97919109A EP0938535B1 EP 0938535 B1 EP0938535 B1 EP 0938535B1 EP 97919109 A EP97919109 A EP 97919109A EP 97919109 A EP97919109 A EP 97919109A EP 0938535 B1 EP0938535 B1 EP 0938535B1
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EP
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Prior art keywords
compound
anhydride
varying
additive
diesel
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EP97919109A
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German (de)
French (fr)
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EP0938535A1 (en
Inventor
Laurent Germanaud
Guy Raoult
Danièle Eber
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Elf Antar France SA
Elf Antar France
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Elf Antar France SA
Elf Antar France
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/22Organic compounds containing nitrogen
    • 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
    • C10L1/221Organic compounds containing nitrogen compounds of uncertain formula; reaction products where mixtures of compounds are obtained
    • 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
    • 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
    • C10L10/00Use of additives to fuels or fires for particular purposes
    • C10L10/18Use of additives to fuels or fires for particular purposes use of detergents or dispersants for purposes not provided for in groups C10L10/02 - C10L10/16

Definitions

  • the present invention relates to an additive bifunctional with detergent and anti-corrosion functions which, when added to engine fuels, considerably reduces problems related to corrosion of parts of the engine and the formation of deposits.
  • Another method of reducing fouling by deposits in engines and in particular on injectors is to add additives to the fuel detergent type whose role is to absorb on metal surfaces to prevent the formation of deposits (preventive effect) and / or eliminate deposits already formed in restoring the cleanliness of the injectors (curative effect).
  • additives used in fuels and even in lubricants, we know more particularly products from the condensation of anhydrides polyalkenylsuccinics on polyamines such as tetraethylenepentamine, described in US Patent 3,172,892. If these additives work well to limit the formation of deposits on new injectors, they remain however not very effective at cleaning injectors already dirty.
  • detergent additives consist of substituted succinic diamides with polyalkylenes, preferably polyisobutenes comprising from 35 to 300 carbon atoms, the resulting diamide condensation of an N-alkylpiperazine secondary amine on either a substituted succinic acid or a anhydride, either an ester or a monoamide derivative; these additives are preferably used in fuels type petrol.
  • the present invention targets a bifunctional additive with detergent properties and anti-corrosion, compatible with other additives usually introduced into fuels, in particular diesel, reducing and even preventing the formation of deposits at the injectors while limiting phenomena corrosion and maintaining good dispersion.
  • the subject of the present invention is a bifunctional additive, for engine fuels, in particular diesel fuels, with detergent and dispersing properties comprising amide or imide functions resulting from the condensation of a compound C consisting of a primary polyamine with a compound A consisting of at least one polyalkenyl carboxylic compound, diacid or anhydride and a compound B consisting of at least one carboxylic compound, monoacid or anhydride, linear or branched, the said additive being characterized in that it is obtained by reacting a compound C of general formula (I) below: H 2 N - [- (CHR 1 - (CH 2 ) p - CHR 2 ) not - NH] m - H in which R 1 and R 2 , identical or different, represent hydrogen or a hydrocarbon group comprising from 1 to 4 carbon atoms, n is an integer varying from 1 to 3, m is an integer varying from 1 to 10 , and p is an integer equal to 0 or 1, on a mixture of the two
  • the compounds A, B and C are used in A / B / C molar ratios preferably corresponding to 1 / (0.1 to 1) / (1 to 3) and are necessarily different from 1/1 / 1. Indeed, there is always an excess of polyamine in the chosen composition which leads to leaving free a certain number of NH 2 terminations of polyamine C.
  • the C / A molar ratio varies from 1.3 to 2.0 and the ratio molar B / A varies from 0.1 to 0.8.
  • the average molar mass of polyalkenyl compounds according to the present invention preferably varies from 200 to 2000 and most often from 200 to 1500. These compounds are well known in the prior art; they are notably obtained by reaction of at least one ⁇ -olefin or at least one chlorinated hydrocarbon, both linear or branched, on maleic acid or anhydride. This olefin or this chlorinated hydrocarbon contains from 10 to 150 carbon atoms in general, preferably 15 to 80 carbon atoms and more often 20 to 75 carbon atoms in their molecule.
  • the olefin can also be an oligomer, such as a dimer, a trimer or a tetramer or a polymer of an olefin lower comprising from 2 to 10 carbon atoms such that ethylene, propylene, n-butene, isobutene, n-hexene, n-octene-1, methyl-2-heptene-1 and propyl-2-propyl-5-hexene-1. Onne would not go beyond the scope of the invention if we mixed several olefins or several chlorinated hydrocarbons.
  • the compounds polyalkenyl carboxyls are chosen from derivatives polyalkenyl succinic acids and anhydrides, the index anhydride varying from 0.5 to 1.2 milli-equivalents of potash per gram of product.
  • succinic anhydrides preferred are n-octadecenyl succinic anhydride, dodecenyl succinic anhydride and anhydrides polyisobutenyl succinics and all anhydrides succinics of weight average molecular weight varying from 200 to 1500.
  • the compound B is preferably chosen from the group consisting of methacrylic acid, acrylic acid, anhydride maleic, succinic anhydride, malonic acid, acid fumaric and adipic acid.
  • polyamines from the group consisting of diethylene triamine, dipropylene triamine, triethylene tetramine, tetraethylene pentamine and their derivatives substituted.
  • product C is added, that is to say the primary polyamine of formula (I) on the mixture of products A and B, i.e. the mixture of carboxylic hydrocarbons.
  • the temperature usually rises between 65 and 250 ° C and preferably between 80 and 200 ° C.
  • the organic solvent necessary for solubilization is chosen for its point boiling range between 65 and 250 ° C and its ability to remove the water formed by condensation of the polyamine on mixture A + B, by azeotropic distillation of the mixture water / solvent.
  • the solvent is preferably chosen from the group consisting of benzene, toluene, xylenes, ethylbenzene and commercial hydrocarbon cuts, for example those distilling from 190 to 209 ° C and containing 99% by weight of aromatic compounds.
  • a mixture of solvents in particular a mixture of xylenes, or another xylene / alcohol mixture, in particular ethyl-2-hexanol on the one hand, to facilitate the homogeneity of the environment and, on the other hand, to favor the kinetics of the reaction.
  • a second object of the invention is a fuel consisting mainly of a middle distillate from a direct distillation cut of crude oil between 150 and 400 ° C or any other index fuel cetane greater than or equal to 30, and for a minor part with the bifunctional additive (s) detergent (s) and anti-corrosion according to the first object of the invention.
  • the concentration of detergent and anti-corrosion additive (s) is greater than 50 ppm, preferably varying from 60 to 600 ppm.
  • the present invention it is possible to add to the said fuel at least one additive from the group of additives oiliness, additives improving the cetane number, demulsifying additives and modifying additives smell.
  • This example describes the preparation of several samples of bifunctional detergent additives and anti-corrosion according to the invention.
  • a mole of polyisobutenyl succinic anhydride A, b moles of compound B, 25 ml of ethyl-2-hexanol and 25 ml of xylene are introduced successively into a 250 ml tetracol flask.
  • the mixture is stirred and heated to 100 ° C. until a homogeneous medium is obtained, then about 5 moles of tetraethylenepentamine or TEPA, C. are added over 5 minutes.
  • the whole is maintained at the same temperature under reflux for three to four hours until a constant volume of extracted water is obtained (1.05 ml).
  • the products obtained have two infrared absorption bands characteristic of the imide functions at 1700 cm -1 and of the amide functions at 1670 cm -1 .
  • This example aims to highlight the improvement detergent properties of samples according to the invention according to the relative concentrations of A, B and C, after addition in diesel fuel. It also aims to highlight the synergistic effect of the combination according to the invention.
  • % Residual flow Average flow rate of injectors at end of test Average flow rate of new injectors ⁇ 100
  • the additives according to the invention give residual flow rates much higher than those of diesel fuel alone and diesel fuel additivated with additives comparative detergents.
  • This example aims to demonstrate the effectiveness of additives according to the invention for cleaning the injectors already fouled (curative effect) compared to additives C according to the procedure described in Example II. Before each test, the injectors are pre-fouled with a diesel without additive for 6 hours according to the procedure described in Example II.
  • Residual flows after the fouling phase with diesel only are those indicated in line 1 of the table II.
  • % efficiency Average flow rate of injectors at end of test Average flow rate of dirty injectors (test flow rate) ⁇ 100 Needle lift (mm) 0.10 0.20 0.30 0.40 0.50 diesel + X 1 230 190 174 158 120 diesel + X 2 243 210 180 170 135 diesel + X 3 260 217 198 172 135 diesel + C 1 164 139 132 135 115 diesel + C 3 207 165 158 145 120
  • This example aims to show the superiority of additives according to the present invention with respect to comparative C additives.
  • Corrosion tests consist in determining the anti-corrosion effect of the additives in diesel fuel on samples of polished ordinary steel in the presence of synthetic seawater according to standard ASTM D665, for a period of 24 hours at the temperature of 60 ° C. They are expressed in% of corroded area. Fuel % of corroded surface Diesel only 100 Diesel + X 1 10 Diesel + X 2 10 Diesel + X 3 5 Diesel + X 4 5 Diesel + C 1 25 Diesel + C 2 60 Diesel + C 3 20
  • the additives according to the invention have excellent properties anti-corrosion, superior to those of known products.

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  • 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)
  • Combustion & Propulsion (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Preventing Corrosion Or Incrustation Of Metals (AREA)
  • Lubricants (AREA)
  • Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)

Abstract

PCT No. PCT/FR97/01634 Sec. 371 Date Jun. 16, 1999 Sec. 102(e) Date Jun. 16, 1999 PCT Filed Sep. 17, 1997 PCT Pub. No. WO98/12283 PCT Pub. Date Mar. 26, 1998The invention concerns a detergent and anti-corrosive additive for engine fuels, in particular gas oil, containing amide or imide functions characterised in that it is obtained by mixing wt. 60 to 90% of a compound A consisting of at least one carboxylic polyalkenyl, diacid or anhydride, of average molecular mass between 200 and 3000, wt. 0.1 to 10% of a compound B consisting of at least one carboxylic compound, monoacid or anhydride, containing 1 to 6 carbon atoms per chain and 10 to 30% of a compound C consisting of at least one primary polyamine of general formula H2N-[-(CHR1-(CH2)p-CHR2)n-NH]m-H, the mol ratios A/B/C corresponding to 1/(0.1 to 1)/(1 to 3), A/B/C never being 1/1/1.

Description

La présente invention concerne un additif bifonctionnel aux fonctions détergente et anti-corrosion qui, ajouté aux carburants moteurs, réduit considérablement les problèmes liés à la corrosion de certaines parties du moteur et à la formation de dépôts.The present invention relates to an additive bifunctional with detergent and anti-corrosion functions which, when added to engine fuels, considerably reduces problems related to corrosion of parts of the engine and the formation of deposits.

En effet, l'utilisation de carburants conventionnels sans additifs détergent et anti-corrosion favorise l'accumulation de dépôts dans le système d'admission, notamment au niveau des injecteurs qui s'encrassent, voire dans la chambre de combustion, consécutif à la présence de composés aromatiques polaires et de traces de lubrifiants.Indeed, the use of conventional fuels without detergent and anti-corrosion additives promotes accumulation of deposits in the intake system, especially at the level of the injectors which get dirty, even in the combustion chamber, following the presence of polar aromatics and traces of lubricants.

L'accumulation de dépôts détériore la qualité de vaporisation du carburant ce qui provoque une augmentation de la consommation, un accroissement des émissions de composés polluants et de fumées, notablement plus importantes au cours de l'accélération, et enfin une augmentation non négligeable du bruit.The accumulation of deposits deteriorates the quality of fuel vaporization which causes an increase consumption, increased emissions of pollutants and smoke, significantly more important during acceleration, and finally a significant increase in noise.

Pour remédier à ce problème de l'encrassement du moteur, il est possible de nettoyer périodiquement les organes encrassés et particulièrement les injecteurs, mais, à la longue, ce procédé devient très onéreux.To remedy this problem of fouling of the motor, it is possible to periodically clean the dirty parts and especially the injectors, but, in the long run, this process becomes very expensive.

Un autre procédé pour réduire l'encrassement par dépôts dans les moteurs et en particulier sur les injecteurs, est d'introduire dans le carburant des additifs de type détergent dont le rôle est de s'absorber sur les surfaces métalliques pour prévenir la formation de dépôts (effet préventif) et/ou d'éliminer les dépôts déjà formés en restaurant la propreté des injecteurs (effet curatif). Ainsi, parmi les additifs utilisés dans les carburants, et même dans les lubrifiants, on connaít plus particulièrement les produits issus de la condensation des anhydrides polyalcénylsucciniques sur des polyamines telles que la tétraéthylènepentamine, décrits dans le brevet US 3.172.892. Si ces additifs donnent de bons résultats pour limiter la formation des dépôts sur des injecteurs neufs, ils demeurent cependant peu efficaces pour nettoyer des injecteurs déjà encrassés.Another method of reducing fouling by deposits in engines and in particular on injectors, is to add additives to the fuel detergent type whose role is to absorb on metal surfaces to prevent the formation of deposits (preventive effect) and / or eliminate deposits already formed in restoring the cleanliness of the injectors (curative effect). Thus, among the additives used in fuels, and even in lubricants, we know more particularly products from the condensation of anhydrides polyalkenylsuccinics on polyamines such as tetraethylenepentamine, described in US Patent 3,172,892. If these additives work well to limit the formation of deposits on new injectors, they remain however not very effective at cleaning injectors already dirty.

D'autres additifs détergents, décrits dans le brevet EP 613.938, sont constitués de diamides succiniques substituées par des polyalkylènes, de préférence des polyisobutènes comprenant de 35 à 300 atomes de carbone, la diamide résultant de la condensation d'une amine secondaire de type N-alkylpipérazine sur soit un acide succinique substitué, soit un anhydride, soit un ester ou une monoamide dérivée ; ces additifs sont de préférence utilisés dans les carburants type essence.Other detergent additives, described in the EP patent 613.938, consist of substituted succinic diamides with polyalkylenes, preferably polyisobutenes comprising from 35 to 300 carbon atoms, the resulting diamide condensation of an N-alkylpiperazine secondary amine on either a substituted succinic acid or a anhydride, either an ester or a monoamide derivative; these additives are preferably used in fuels type petrol.

En outre, de tels composés sont connus pour leurs propriétés dispersantes dans les lubrifiants comme le décrit le brevet EP 72.645.In addition, such compounds are known for their dispersing properties in lubricants as described in Patent EP 72,645.

Cependant, si ces composés sont bons détergents, ils n'empêchent pas totalement la formation de dépôt et ont un effet curatif limité, voire nul. Ainsi, la présente invention vise un additif bifonctionnel aux propriétés détergentes et anti-corrosion, compatible avec les autres additifs usuellement introduits dans les carburants, en particulier les gazoles, permettant de réduire et même d'empêcher la formation des dépôts au niveau des injecteurs tout en limitant les phénomènes de corrosion et en maintenant une bonne dispersion.However, if these compounds are good detergents, they do not completely prevent deposit formation and have a limited or even no curative effect. Thus, the present invention targets a bifunctional additive with detergent properties and anti-corrosion, compatible with other additives usually introduced into fuels, in particular diesel, reducing and even preventing the formation of deposits at the injectors while limiting phenomena corrosion and maintaining good dispersion.

Dans le brevet US 5.034.018, sont décrits des additifs carburants visant à limiter l'encrassement au niveau des injecteurs d'un moteur à combustion interne obtenus à partir de composés amido-amines comprenant des extrémités NH2 libres sur lesquelles ont fait réagir des composés mono et dicarboxyliques de façon à préparer des amido-imides.In US patent 5,034,018, fuel additives are described which aim to limit fouling at the level of the injectors of an internal combustion engine obtained from amido-amine compounds comprising free NH 2 ends on which reacted mono and dicarboxylic compounds so as to prepare amidoimides.

La présente invention a pour objet un additif bifonctionnel, pour carburants moteur, notamment les carburants de type gazole, aux propriétés détergentes et dispersantes comprenant des fonctions amides ou imides résultant de la condensation d'un composé C constitué d'une polyamine primaire avec un composé A constitué par au moins un composé polyalcényl carboxylique, diacide ou anhydride et un composé B constitué par au moins un composé carboxylique, monoacide ou anhydride, linéaire ou ramifié, le dit additif étant caractérisé en ce qu'il est obtenu en faisant réagir un composé C de formule générale (I) ci-après : H2N - [-(CHR1- (CH2)p - CHR2)n - NH]m- H dans laquelle R1 et R2, identiques ou différents, représentent l'hydrogène ou un groupement hydrocarboné comprenant de 1 à 4 atomes de carbone, n est un nombre entier variant de 1 à 3, m est un nombre entier variant de 1 à 10, et p est un nombre entier égal à 0 ou 1, sur un mélange des deux composés A et B contenu dans un solvant organique de point d'ébullition compris entre 65 et 250 °C, le composé A, un composé polyalcényl carboxylique comprenant de 2 à 20 atomes de carbone par groupement alcényl linéaire ou ramifié et ayant une masse moléculaire moyenne variant de 200 à 3000, et le composé B étant choisi dans le groupe constitué par l'acide méthacrylique, l'acide acrylique, l'anhydride maléique et l'anhydride succinique.The subject of the present invention is a bifunctional additive, for engine fuels, in particular diesel fuels, with detergent and dispersing properties comprising amide or imide functions resulting from the condensation of a compound C consisting of a primary polyamine with a compound A consisting of at least one polyalkenyl carboxylic compound, diacid or anhydride and a compound B consisting of at least one carboxylic compound, monoacid or anhydride, linear or branched, the said additive being characterized in that it is obtained by reacting a compound C of general formula (I) below: H 2 N - [- (CHR 1 - (CH 2 ) p - CHR 2 ) not - NH] m - H in which R 1 and R 2 , identical or different, represent hydrogen or a hydrocarbon group comprising from 1 to 4 carbon atoms, n is an integer varying from 1 to 3, m is an integer varying from 1 to 10 , and p is an integer equal to 0 or 1, on a mixture of the two compounds A and B contained in an organic solvent with a boiling point of between 65 and 250 ° C., the compound A, a polyalkenyl carboxylic compound comprising 2 to 20 carbon atoms per linear or branched alkenyl group and having an average molecular mass varying from 200 to 3000, and compound B being chosen from the group consisting of methacrylic acid, acrylic acid, maleic anhydride and succinic anhydride.

Selon l'invention, les composés A, B et C sont utilisés dans des rapports molaires A/B/C correspondant de préférence à 1/ (0,1 à 1)/ (1 à 3) et sont nécessairement différents de 1/1/1. En effet, il y a toujours un excès de polyamine dans la composition choisie ce qui conduit à laisser libres un certain nombre de terminaisons NH2 de la polyamine C. De préférence, le rapport molaire C/A varie de 1.3 à 2.0 et le rapport molaire B/A varie de 0.1 à 0.8.According to the invention, the compounds A, B and C are used in A / B / C molar ratios preferably corresponding to 1 / (0.1 to 1) / (1 to 3) and are necessarily different from 1/1 / 1. Indeed, there is always an excess of polyamine in the chosen composition which leads to leaving free a certain number of NH 2 terminations of polyamine C. Preferably, the C / A molar ratio varies from 1.3 to 2.0 and the ratio molar B / A varies from 0.1 to 0.8.

Comparé aux additifs connus, la combinaison de composés mono et dicarboxyliques en plus d'une polyamine, favorise la détergence et l'effet anti-corrosion des additifs selon l'invention. Il correspond à un effet synergique de la combinaison de ces trois composants entre eux. Compared to known additives, the combination of compounds mono and dicarboxyls in addition to a polyamine, promotes detergency and anti-corrosion effect of additives according to the invention. It corresponds to a synergistic effect of combination of these three components together.

La masse molaire moyenne des composés polyalcényl carboxyliques selon la présente invention varie de préférence de 200 à 2000 et le plus souvent de 200 à 1500. Ces composés sont bien connus de l'art antérieur ; ils sont notamment obtenus par réaction d'au moins une α-oléfine ou d'au moins un hydrocarbure chloré, l'un et l'autre linéaire ou ramifié, sur l'acide ou l'anhydride maléique. Cette oléfine ou cet hydrocarbure chloré comprend de 10 à 150 atomes de carbone en général, de préférence 15 à 80 atomes de carbone et le plus souvent de 20 à 75 atomes de carbone dans leur molécule. L'oléfine peut être également un oligomère, tel qu'un dimère, un trimère ou un tétramère ou encore un polymère d'une oléfine inférieure comprenant de 2 à 10 atomes de carbone telle que l'éthylène, le propylène, le n-butène, l'isobutène, le n-hexène, le n-octène-1, le méthyl-2-heptène-1 et le propyl-2-propyl-5-héxène-1. On ne sortirait pas du cadre de l'invention si on mélangeait plusieurs oléfines ou plusieurs hydrocarbures chlorés.The average molar mass of polyalkenyl compounds according to the present invention preferably varies from 200 to 2000 and most often from 200 to 1500. These compounds are well known in the prior art; they are notably obtained by reaction of at least one α-olefin or at least one chlorinated hydrocarbon, both linear or branched, on maleic acid or anhydride. This olefin or this chlorinated hydrocarbon contains from 10 to 150 carbon atoms in general, preferably 15 to 80 carbon atoms and more often 20 to 75 carbon atoms in their molecule. The olefin can also be an oligomer, such as a dimer, a trimer or a tetramer or a polymer of an olefin lower comprising from 2 to 10 carbon atoms such that ethylene, propylene, n-butene, isobutene, n-hexene, n-octene-1, methyl-2-heptene-1 and propyl-2-propyl-5-hexene-1. Onne would not go beyond the scope of the invention if we mixed several olefins or several chlorinated hydrocarbons.

Dans un mode préféré de l'invention, les composés polyalcényl carboxyliques sont choisis parmi les dérivés acides et anhydrides polyalcényl succiniques, l'indice d'anhydride variant de 0,5 à 1.2 milli-équivalents de potasse par gramme de produit.In a preferred embodiment of the invention, the compounds polyalkenyl carboxyls are chosen from derivatives polyalkenyl succinic acids and anhydrides, the index anhydride varying from 0.5 to 1.2 milli-equivalents of potash per gram of product.

Parmi les anhydrides succiniques, les anhydrides préférés sont l'anhydride n-octadécényl succinique, l'anhydride dodécényl succinique et les anhydrides polyisobutènyl succiniques et tous les anhydrides succiniques de masse moléculaire moyenne en poids variant de 200 à 1500.Among the succinic anhydrides, the anhydrides preferred are n-octadecenyl succinic anhydride, dodecenyl succinic anhydride and anhydrides polyisobutenyl succinics and all anhydrides succinics of weight average molecular weight varying from 200 to 1500.

Dans un mode préféré de l'invention, le composé B est choisi de préférence dans le groupe constitué par l'acide méthacrylique, l'acide acrylique, l'anhydride maléique, l'anhydride succinique, l'acide malonique, l'acide fumarique et l'acide adipique.In a preferred embodiment of the invention, the compound B is preferably chosen from the group consisting of methacrylic acid, acrylic acid, anhydride maleic, succinic anhydride, malonic acid, acid fumaric and adipic acid.

Parmi les polyamines primaires selon la formule (I), on préfère les polyamines du groupe constitué par la diéthylène triamine, la dipropylène triamine, la triéthylène tétramine, la tétraéthylène pentamine et leurs dérivés substitués.Among the primary polyamines according to formula (I), polyamines from the group consisting of diethylene triamine, dipropylene triamine, triethylene tetramine, tetraethylene pentamine and their derivatives substituted.

Le mélange de ces composés A, B et C peut se faire indifféremment dans cet ordre ou dans un ordre différent. Cependant, dans un mode préféré, on ajoute le produit C, c'est-à-dire la polyamine primaire de formule (I) sur le mélange des produits A et B, c'est-à-dire le mélange d'hydrocarbures carboxyliques. On opère habituellement en introduisant de façon progressive la polyamine C à une solution dans un solvant organique de ce mélange d'hydrocarbures carboxyliques à température ordinaire, puis la température est montée habituellement entre 65 et 250 °C et de préférence entre 80 et 200 °C. Le solvant organique nécessaire à la solubilisation est choisi pour son point d'ébullition compris entre 65 et 250 °C et sa capacité à éliminer l'eau formée par condensation de la polyamine sur le mélange A+B, par distillation azéotropique du mélange eau/solvant. Le solvant est de préférence choisi dans le groupe constitué par le benzène, le toluène, les xylènes, l'éthylbenzène et les coupes commerciales d'hydrocarbures, par exemple ceux distillant de 190 à 209 °C et contenant 99% en poids de composés aromatiques. Bien entendu, on ne sortirait pas du cadre de l'invention, si on utilisait un mélange de solvants, notamment un mélange de xylènes, ou encore un mélange xylène/alcool, en particulier l'éthyl-2-hexanol pour d'une part, faciliter l'homogénéité du milieu et, d'autre part, favoriser la cinétique de la réaction. Après la fin de l'addition de la polyamine primaire C, on maintient le chauffage sous reflux jusqu'à l'élimination complète de l'eau contenue, habituellement pendant de 0,5 à 7 heures, de préférence de 1 à 5 heures.The mixing of these compounds A, B and C can be done either in this order or in a different order. However, in a preferred mode, product C is added, that is to say the primary polyamine of formula (I) on the mixture of products A and B, i.e. the mixture of carboxylic hydrocarbons. We usually operate in gradually introducing polyamine C to a solution in an organic solvent of this mixture of carboxylic hydrocarbons at ordinary temperature, then the temperature usually rises between 65 and 250 ° C and preferably between 80 and 200 ° C. The organic solvent necessary for solubilization is chosen for its point boiling range between 65 and 250 ° C and its ability to remove the water formed by condensation of the polyamine on mixture A + B, by azeotropic distillation of the mixture water / solvent. The solvent is preferably chosen from the group consisting of benzene, toluene, xylenes, ethylbenzene and commercial hydrocarbon cuts, for example those distilling from 190 to 209 ° C and containing 99% by weight of aromatic compounds. Of course, we don't would not go beyond the scope of the invention, if a mixture of solvents, in particular a mixture of xylenes, or another xylene / alcohol mixture, in particular ethyl-2-hexanol on the one hand, to facilitate the homogeneity of the environment and, on the other hand, to favor the kinetics of the reaction. After the addition of the primary polyamine C has been completed, keeps heating under reflux until elimination complete with water contained, usually for 0.5 to 7 hours, preferably 1 to 5 hours.

Un deuxième objet de l'invention est un carburant constitué pour une majeure partie par un distillat moyen issu d'une coupe de distillation directe de pétrole brut compris entre 150 et 400°C ou tout autre carburant d'indice de cétane supérieur ou égal à 30, et pour une partie mineure par le ou les additif(s) bifonctionnel(s) détergent(s) et anti-corrosion selon le premier objet de l'invention.A second object of the invention is a fuel consisting mainly of a middle distillate from a direct distillation cut of crude oil between 150 and 400 ° C or any other index fuel cetane greater than or equal to 30, and for a minor part with the bifunctional additive (s) detergent (s) and anti-corrosion according to the first object of the invention.

Dans un mode préféré de ce carburant, la concentration en additif(s) détergent et anti-corrosion est supérieure à 50 ppm, de préférence variant de 60 à 600 ppm.In a preferred mode of this fuel, the concentration of detergent and anti-corrosion additive (s) is greater than 50 ppm, preferably varying from 60 to 600 ppm.

Selon la présente invention, on peut ajouter au dit carburant au moins un additif du groupe des additifs d'onctuosité, des additifs améliorant l'indice de cétane, des additifs désémulsifiants et des additifs modificateurs d'odeur.According to the present invention, it is possible to add to the said fuel at least one additive from the group of additives oiliness, additives improving the cetane number, demulsifying additives and modifying additives smell.

Les exemples ci-après visent à illustrer l'invention sans en limiter la portée. The examples below are intended to illustrate the invention without limiting its scope.

EXEMPLE IEXAMPLE I

Le présent exemple décrit la préparation de plusieurs échantillons d'additifs bifonctionnels détergents et anti-corrosion selon l'invention.This example describes the preparation of several samples of bifunctional detergent additives and anti-corrosion according to the invention.

Ces échantillons selon l'invention sont référencés Xi et les exemples comparatifs C1, i correspondant à une numérotation permettant de les différencier.These samples according to the invention are referenced X i and the comparative examples C 1 , i corresponding to a numbering making it possible to differentiate them.

La composition de ces échantillons est donné dans le tableau I ci-après : Echantillon A B C C/A B/A C/B 4 Nature a (moles) Nature b (moles) nature c (moles) X1 A1 0.03 AMA 0.01 TEPA 0.04 1.33 0.33 4 X2 A1 0.03 AS 0.01 TEPA 0.04 1.33 0.33 4 X3 A2 0.03 AMA 0.01 TEPA 0.04 1.33 0.33 4 X4 A1 0.03 AMA 0.01 TEPA 0.042 1.4 0.33 4.2 X5 A1 0.03 AMA 0.01 TEPA 0.05 1.6 0.33 5 X5 A1 0.03 AMA 0.02 TEPA 0.048 1.6 0.60 5.8 X7 A1 0.03 AMA 0.01 TEPA 0.054 1.8 0.33 5.4 X8 A1 0.03 AS 0.01 TEPA 0.06 2 0.33 6 X9 A1 0.03 AS 0.015 TEPA 0.79 2.4 0.45 7.9 X10 A1 0.03 AMA 0.025 TEPA 0.04 1.3 0.8 1.6 C1 A1 0.03 TEPA 0.03 1 C2 AMA 0.1 TEPA 0.1 1 C3 A1 0.03 AMA 0.03 TEPA 0.03 1 1 1 A1= anhydride polyisobutènylsuccinique de masse moléculaire moyenne 950 et d'indice d'anhydride égal à 0,7 milli-équivalent de potasse par gramme A2= anhydride polyisobutènylsuccinique de masse moléculaire moyenne 950 et d'indice d'anhydride égal à 0,8 milli-équivalent de potasse par gramme, commercialisé sous la référence ADX 104 par la société ADIBIS. AMA= acide méthacrylique AS= anhydride succinique TEPA= tétraéthylène pentamine The composition of these samples is given in Table I below: Sample AT B VS IT B / A C / B 4 Nature a (moles) Nature b (moles) nature c (moles) X 1 At 1 0.03 WADA 0.01 TEPA 0.04 1.33 0.33 4 X 2 At 1 0.03 AS 0.01 TEPA 0.04 1.33 0.33 4 X 3 A 2 0.03 WADA 0.01 TEPA 0.04 1.33 0.33 4 X 4 At 1 0.03 WADA 0.01 TEPA 0042 1.4 0.33 4.2 X 5 At 1 0.03 WADA 0.01 TEPA 0.05 1.6 0.33 5 X 5 At 1 0.03 WADA 0.02 TEPA 0048 1.6 0.60 5.8 X 7 At 1 0.03 WADA 0.01 TEPA 0054 1.8 0.33 5.4 X 8 At 1 0.03 AS 0.01 TEPA 0.06 2 0.33 6 X 9 At 1 0.03 AS 0015 TEPA 0.79 2.4 0.45 7.9 X 10 At 1 0.03 WADA 0025 TEPA 0.04 1.3 0.8 1.6 C 1 At 1 0.03 TEPA 0.03 1 C 2 WADA 0.1 TEPA 0.1 1 C 3 At 1 0.03 WADA 0.03 TEPA 0.03 1 1 1 A 1 = polyisobutenyl succinic anhydride with an average molecular weight of 950 and an anhydride index equal to 0.7 milli-equivalent of potash per gram A 2 = polyisobutenyl succinic anhydride with an average molecular weight of 950 and an anhydride index equal to 0.8 milli-equivalent of potassium hydroxide per gram, sold under the reference ADX 104 by the company ADIBIS. AMA = methacrylic acid AS = succinic anhydride TEPA = tetraethylene pentamine

Les échantillons X1 rassemblés dans ce tableau I sont obtenus selon la procédure suivante.The samples X 1 collected in this table I are obtained according to the following procedure.

On introduit successivement dans un ballon tétracol de 250 ml, a moles d'anhydride polyisobutènylsuccinique A, b moles du composé B, 25 ml d'éthyl-2-hexanol et 25 ml de xylène. Le mélange est agité et chauffé à 100°C jusqu'à obtenir un milieu homogène, puis on ajoute en 5 minutes environ c moles de tétraéthylènepentamine ou TEPA,C. L'ensemble est maintenu à la même température sous reflux pendant trois à quatre heures jusqu'à l'obtention d'un volume constant d'eau extraite ( 1,05 ml). Les produits obtenus présentent deux bandes d'absorption infra-rouge caractéristiques des fonctions imides à 1700 cm-1 et des fonctions amides à 1670 cm-1.A mole of polyisobutenyl succinic anhydride A, b moles of compound B, 25 ml of ethyl-2-hexanol and 25 ml of xylene are introduced successively into a 250 ml tetracol flask. The mixture is stirred and heated to 100 ° C. until a homogeneous medium is obtained, then about 5 moles of tetraethylenepentamine or TEPA, C. are added over 5 minutes. The whole is maintained at the same temperature under reflux for three to four hours until a constant volume of extracted water is obtained (1.05 ml). The products obtained have two infrared absorption bands characteristic of the imide functions at 1700 cm -1 and of the amide functions at 1670 cm -1 .

Pour les exemples comparatifs C1, C2 et C3, on opère comme précédemment pour les échantillons Xi, mais en modifiant les proportions en composés A, B et C. Par spectroscopie infra-rouge, on observe des bandes caractéristiques d'absorption des imides à 1700cm-1 (intense) et des amides à 1670cm-1 (faible).For the comparative examples C 1 , C 2 and C 3 , the operation is carried out as above for the samples X i , but by modifying the proportions in compounds A, B and C. By infrared spectroscopy, characteristic absorption bands are observed imides at 1700cm -1 (intense) and amides at 1670cm -1 (weak).

EXEMPLE IIEXAMPLE II

Le présent exemple vise à souligner l'amélioration des propriétés détergentes des échantillons selon l'invention selon les concentrations relatives en A, B et C, après addition dans un carburant gazole. Il vise également à souligner l'effet de synergie du à la combinaison selon l'invention.This example aims to highlight the improvement detergent properties of samples according to the invention according to the relative concentrations of A, B and C, after addition in diesel fuel. It also aims to highlight the synergistic effect of the combination according to the invention.

Le gazole utilisé est un gazole moteur dont les caractéristiques principales sont :

  • densité à 15 °C = 0,836 Kg/l
  • point initial de distillation =174°C
  • point final de distillation = 366°C
  • indice de cétane = 53
  • teneur en soufre = 0,24 % poids.
The diesel fuel used is a diesel engine whose main characteristics are:
  • density at 15 ° C = 0.836 Kg / l
  • initial distillation point = 174 ° C
  • distillation end point = 366 ° C
  • cetane number = 53
  • sulfur content = 0.24% by weight.

Les essais ont été réalisés sur le gazole moteur seul ou additivé avec l'un des additifs Xi selon l'invention ou les détergents comparatifs Ci, à une concentration en poids de matière active de 175 ppm.The tests were carried out on diesel fuel alone or additivated with one of the additives X i according to the invention or the comparative detergents C i , at a concentration by weight of active material of 175 ppm.

Ces essais consistent à suivre la procédure d'essai moteur telle que décrite dans la littérature publiée par la SAE (Society for Automotive Engineers) sous la référence SAE # 922184 de 1992. Ils sont réalisés sur un ensemble de deux groupes électrogènes Kubota Z 600 B entraínés par des moteurs Diesel bicylindres de 570 cm3 à 4 temps et à injection indirecte.These tests consist in following the engine test procedure as described in the literature published by the SAE (Society for Automotive Engineers) under the reference SAE # 922184 of 1992. They are carried out on a set of two Kubota Z 600 B generator sets driven by 570 cc 3- stroke 4-stroke diesel engines with indirect injection.

Chaque essai est mené pendant une durée de 6 heures dans les conditions suivantes :

  • régime moteur : 3000 t/mn
  • charge : 2/3 de la charge maximale.
Each test is carried out for a period of 6 hours under the following conditions:
  • engine speed: 3000 rpm
  • load: 2/3 of the maximum load.

Au début de chaque essai, les moteurs sont équipés d'injecteurs neufs dont les débits ont été mesurés préalablement à leur installation, à différentes levées d'aiguille des injecteurs. A la fin de chaque essai, les injecteurs sont démontés, et leurs débits sont mesurés pour les mêmes levées d'aiguille. L'efficacité des additifs détergents testés est comparée à partir de leur pourcentage de débit résiduel (%dr) calculé par la formule ci-après. % Débit résiduel = Débit moyen des injecteurs fin d'essai Débit moyen des injecteurs neufs × 100 At the start of each test, the engines are fitted with new injectors, the flow rates of which were measured prior to their installation, at different needle liftings from the injectors. At the end of each test, the injectors are disassembled, and their flow rates are measured for the same needle lifts. The effectiveness of the detergent additives tested is compared on the basis of their percentage of residual flow rate (% dr) calculated by the formula below. % Residual flow = Average flow rate of injectors at end of test Average flow rate of new injectors × 100

Le tableau II ci-après rassemble les résultats obtenus. Levée d'aiguille(mm) 0,05 0,10 0,20 0,30 0,40 0,50 Gazole seul 10 14 23 31 40 54 gazole + X1 48 53 62 73 83 88 gazole + X2 50 59 78 87 92 93 gazole + X3 77 80 89 92 93 93 gazole + X4 54 60 70 80 86 91 gazole + X5 64 74 82 89 93 95 gazole + X6 67 78 83 88 91 92 gazole + X7 79 85 92 94 95 95 gazole + X8 68 78 91 95 95 95 gazole + X9 30 34 45 56 65 69 gazole + X10 35 39 49 57 68 72 gazole + C1 34 38 48 58 67 73 gazole + C2 0 0 0 0 0 0 gazole + C3 18 22 33 42 54 65 Table II below collates the results obtained. Needle lift (mm) 0.05 0.10 0.20 0.30 0.40 0.50 Diesel only 10 14 23 31 40 54 diesel + X 1 48 53 62 73 83 88 diesel + X 2 50 59 78 87 92 93 diesel + X 3 77 80 89 92 93 93 diesel + X 4 54 60 70 80 86 91 diesel + X 5 64 74 82 89 93 95 diesel + X6 67 78 83 88 91 92 diesel + X 7 79 85 92 94 95 95 diesel + X 8 68 78 91 95 95 95 diesel + X 9 30 34 45 56 65 69 diesel + X 10 35 39 49 57 68 72 diesel + C 1 34 38 48 58 67 73 diesel + C 2 0 0 0 0 0 0 diesel + C 3 18 22 33 42 54 65

Comme le montre le tableau I, les additifs selon l'invention donnent des débits résiduels bien supérieurs à ceux du gazole seul et du gazole additivé par des additifs détergents comparatifs.As shown in Table I, the additives according to the invention give residual flow rates much higher than those of diesel fuel alone and diesel fuel additivated with additives comparative detergents.

EXEMPLE IIIEXAMPLE III

Le présent exemple vise à démontrer l'efficacité des additifs selon l'invention pour le nettoyage des injecteurs déjà encrassés (effet curatif) comparé aux additifs C selon la procédure décrite dans l'exemple II. Préalablement à chaque essai, les injecteurs sont pré-encrassés avec un gazole sans additif pendant 6 heures selon la procédure décrite dans l'exemple II.This example aims to demonstrate the effectiveness of additives according to the invention for cleaning the injectors already fouled (curative effect) compared to additives C according to the procedure described in Example II. Before each test, the injectors are pre-fouled with a diesel without additive for 6 hours according to the procedure described in Example II.

Les débits résiduels après la phase d'encrassement avec le gazole seul sont ceux indiqués dans la ligne 1 du tableau II. Residual flows after the fouling phase with diesel only are those indicated in line 1 of the table II.

L'efficacité des additifs à nettoyer les injecteurs déjà encrassés est calculée d'après la formule suivante : % efficacité = Débit moyen des injecteurs fin d'essai Débit moyen des injecteurs encrassés (débit d'essai) × 100 Levée d'aiguille(mm) 0,10 0,20 0,30 0,40 0,50 gazole + X1 230 190 174 158 120 gazole + X2 243 210 180 170 135 gazole + X3 260 217 198 172 135 gazole + C1 164 139 132 135 115 gazole + C3 207 165 158 145 120 The efficiency of the additives for cleaning already dirty injectors is calculated according to the following formula: % efficiency = Average flow rate of injectors at end of test Average flow rate of dirty injectors (test flow rate) × 100 Needle lift (mm) 0.10 0.20 0.30 0.40 0.50 diesel + X 1 230 190 174 158 120 diesel + X 2 243 210 180 170 135 diesel + X 3 260 217 198 172 135 diesel + C 1 164 139 132 135 115 diesel + C 3 207 165 158 145 120

Les résultats d'efficacité des additifs au regard du nettoyage des injecteurs encrassés, rassemblés dans le tableau III sont donnés pour chaque levée d'aiguille ; ils montrent encore la supériorité des additifs selon l'invention.Efficacy results of additives with regard to cleaning of dirty injectors, collected in the Table III are given for each needle lift; they still show the superiority of additives according to the invention.

EXEMPLE IVEXAMPLE IV

Le présent exemple vise à montrer la supériorité des additifs selon la présente invention par rapport aux additifs C comparatifs.This example aims to show the superiority of additives according to the present invention with respect to comparative C additives.

Les essais de corrosion consistent à déterminer l'effet anti-corrosif des additifs dans le gazole sur des échantillons d'acier ordinaire poli en présence d'eau de mer synthétique selon la norme ASTM D665, pendant une durée de 24 heures à la température de 60°C. Ils sont exprimés en % de surface corrodée. Carburant % de surface corrodée Gazole seul 100 Gazole + X1 10 Gazole + X2 10 Gazole + X3 5 Gazole + X4 5 Gazole + C1 25 Gazole + C2 60 Gazole + C3 20 Corrosion tests consist in determining the anti-corrosion effect of the additives in diesel fuel on samples of polished ordinary steel in the presence of synthetic seawater according to standard ASTM D665, for a period of 24 hours at the temperature of 60 ° C. They are expressed in% of corroded area. Fuel % of corroded surface Diesel only 100 Diesel + X 1 10 Diesel + X 2 10 Diesel + X 3 5 Diesel + X 4 5 Diesel + C 1 25 Diesel + C 2 60 Diesel + C 3 20

Comme le montre les résultats du tableau IV, les additifs selon l'invention ont d'excellentes propriétés anti-corrosion, supérieures à celles des produits connus.As shown in the results in Table IV, the additives according to the invention have excellent properties anti-corrosion, superior to those of known products.

Claims (7)

  1. Detergent and corrosion-inhibiting additive for engine fuels, in particular fuels of diesel type, comprising amide or imide functional groups resulting from the condensation of a compound C, composed of a primary polyamine, with a compound A, composed of at least one polyalkenylcarboxylic diacid or anhydride compound, and a compound B, composed of at least one linear or branched carboxylic monoacid or anhydride compound, the said additive being characterized in that it is obtained by reacting compound C of general formula (I) below: H2N- [- (CHR1- (CH2)p - CHR2)n - NH]m - H    in which R1 and R2, which are identical or different, represent hydrogen or a hydrocarbon group comprising from 1 to 4 carbon atoms, n is an integer varying from 1 to 3, m is an integer varying from 1 to 10 and p is an integer equal to 0 or 1, on a mixture of two compounds A and B contained in an organic solvent with a boiling point comprised between 65 and 250°C, compound A being a carboxylic polyalkenyl compound comprising from 2 to 20 carbon atoms per linear or branched alkenyl group and having a mean molecular weight varying from 200 to 3000, and the compound B being selected from the group consisting of methacrylic acid, acrylic acid, maleic hydride and succinic anhydride, the molar ratios of A, B and C being such that A/B/C corresponds to 1/(0.1 to 1)/(1 to 3), it never being possible for A/B/C to be 1/1/1, the molar ratio C/A varying from 1.3 to 2.0, and the molar ratio B/A varying from 0.1 to 0.8.
  2. Additive according to Claim 1, characterized in that the average molar mass of the polyalkenylcarboxylic compounds A varies from 200 to 2,000 and preferably from 200 to 1,500.
  3. Additive according to one of Claims 1 to 2, characterized in that the polyalkenylcarboxyliccompounds are chosen from polyalkenylsuccinic acid and anhydride derivatives with an anhydride number varying from 0.5 to 1.2 milliequivalents of potassium hydroxide per gram of compound.
  4. Additive according to one of Claims 1 to 3, characterized in that the succinic anhydrides are chosen from the group composed of n-octadecenylsuccinic anhydride, dodecenylsuccinic anhydride and polyisobutenylsuccinic anhydrides, and any succinic anhydride with a weight-average molecular mass varying from 200 to 1,500.
  5. Additive according to one of Claims 1 to 4, characterized in that the primary polyamines are polyamines from the group composed of diethylenetriamine, dipropylenetriamine, triethylenetetramine, tetraethylenepentamine and their substituted derivatives.
  6. Fuel mostly comprising at least one middle distillate resulting from a crude oil direct distillation cut of between 150 and 400°C or any other fuel with a cetane number higher than or equal to 30 and comprising, to a minor extent, at least one additive according to one of Claims 1 to 5.
  7. Fuel according to Claim 6, characterized in that it contains at least 50 ppm, and preferably from 60 to 600 ppm, of the detergent and corrosion-inhibiting additive or additives.
EP97919109A 1996-09-18 1997-09-17 Detergent and anti-corrosive additive for fuels and fuel composition Expired - Lifetime EP0938535B1 (en)

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FR9611388 1996-09-18
FR9611388A FR2753455B1 (en) 1996-09-18 1996-09-18 DETERGENT AND ANTI-CORROSION ADDITIVE FOR FUELS AND FUEL COMPOSITION
PCT/FR1997/001634 WO1998012283A1 (en) 1996-09-18 1997-09-17 Detergent and anti-corrosive additive for fuels and fuel composition

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CA2266522C (en) 2005-07-26
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US6083287A (en) 2000-07-04
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KR20000036209A (en) 2000-06-26
HUP9903777A3 (en) 2001-10-29
WO1998012283A1 (en) 1998-03-26
JP3763584B2 (en) 2006-04-05
ES2170386T3 (en) 2002-08-01
KR100467280B1 (en) 2005-01-24
DE69710913T2 (en) 2002-10-31
RU2165448C2 (en) 2001-04-20
EP0938535A1 (en) 1999-09-01
MY116976A (en) 2004-04-30
JP2001503081A (en) 2001-03-06
FR2753455A1 (en) 1998-03-20
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ATE214085T1 (en) 2002-03-15
CA2266522A1 (en) 1998-03-26
HU223377B1 (en) 2004-06-28
HUP9903777A2 (en) 2000-04-28
DK0938535T3 (en) 2002-06-24

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