EP0422986A1 - Process for the preparation of dielectric fluids - Google Patents

Process for the preparation of dielectric fluids Download PDF

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Publication number
EP0422986A1
EP0422986A1 EP19900402722 EP90402722A EP0422986A1 EP 0422986 A1 EP0422986 A1 EP 0422986A1 EP 19900402722 EP19900402722 EP 19900402722 EP 90402722 A EP90402722 A EP 90402722A EP 0422986 A1 EP0422986 A1 EP 0422986A1
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Prior art keywords
aromatic
dielectric
condensation
products
toluene
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German (de)
French (fr)
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EP0422986B1 (en
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Raymond Commandeur
Noelle Berger
Pierre Jay
Jacques Kervennal
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Arkema France SA
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Elf Atochem SA
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Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01BCABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
    • H01B3/00Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties
    • H01B3/18Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances
    • H01B3/20Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances liquids, e.g. oils
    • H01B3/22Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances liquids, e.g. oils hydrocarbons
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M105/00Lubricating compositions characterised by the base-material being a non-macromolecular organic compound
    • C10M105/02Well-defined hydrocarbons
    • C10M105/06Well-defined hydrocarbons aromatic
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M105/00Lubricating compositions characterised by the base-material being a non-macromolecular organic compound
    • C10M105/50Lubricating compositions characterised by the base-material being a non-macromolecular organic compound containing halogen
    • C10M105/52Lubricating compositions characterised by the base-material being a non-macromolecular organic compound containing halogen containing carbon, hydrogen and halogen only
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2203/00Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
    • C10M2203/06Well-defined aromatic compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2211/00Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions
    • C10M2211/02Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions containing carbon, hydrogen and halogen only
    • C10M2211/024Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions containing carbon, hydrogen and halogen only aromatic
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10MLUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
    • C10M2211/00Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions
    • C10M2211/06Perfluorinated compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/14Electric or magnetic purposes
    • C10N2040/16Dielectric; Insulating oil or insulators
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10NINDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
    • C10N2040/00Specified use or application for which the lubricating composition is intended
    • C10N2040/14Electric or magnetic purposes
    • C10N2040/17Electric or magnetic purposes for electric contacts

Definitions

  • the present invention relates to a process for the synthesis of dielectric fluids and more particularly to an improvement of the processes comprising a condensation of the FRIEDEL and CRAFTS type catalyzed by ferric chloride.
  • dielectric liquids of the formula have been described in which n, x, y and z have the value 1 or 2.
  • These products can be prepared by condensation of: in which n, x, y and z have the same meaning as above in the presence of a catalyst from FRIEDEL and CRAFTS. After the condensation, the catalyst is destroyed, for example by adding a dilute aqueous solution of hydrochloric acid followed by washing the organic phase.
  • Patent application EP 136230 describes dielectric fluids which are polyarylalkane oligomers obtained by condensation of benzyl chloride C6H5CH2Cl and benzylidene chloride C6H5CHCl2 on toluene in the presence of a FRIEDEL and CRAFTS catalyst.
  • the Applicant has made the same observation as for the process of the EP 8251 application cited above, that is to say that by using ferric chloride, it is possible to omit the washing step and yet produce a fluid capable of dielectric.
  • the Applicant has found a particularly simple process for synthesizing dielectric fluids by condensation of the FRIEDEL and CRAFTS type.
  • step a is a reaction of FRIEDEL and CRAFTS.
  • Aromatic halides denote, for example, alkylbenzene or (polyalkyl) benzene having at least one halogen in the benzyl position on the alkyl chain
  • the benzated nucleus nique can, in addition to halogenated alkyl chains, be substituted by halogens, alkyls having up to three carbon atoms or nitrile or NO2 groups.
  • the alkyl chains which carry at least one halogen can be identical or different and contain up to three carbon atoms.
  • aromatic halides can be, for example, the products of formulas:
  • aromatic halides are condensed with aromatic compounds.
  • aromatic compounds denote, for example, benzene which can be substituted by one or more identical or different alkyl groups and having up to 8 carbon atoms, halogens or nitrile or NO2 groups.
  • aromatic compounds can be, for example, benzene, toluene, xylene, products of formula:
  • the condensation of the step takes place in practice at a temperature between 50 ° C and 150 ° C.
  • the amount of ferric chloride is usually between 50 ppm and 1% by weight of the reaction mass.
  • an excess of the aromatic halide or an excess of the aromatic compound can be used.
  • different condensation products are obtained, which are themselves mixtures. Most often, it may be necessary to distill the excess reagents (step c ) because these products, even in admixture with the condensation products do not have dielectric properties or cannot be used as dielectrics because of their too much volatility.
  • step d all or at least one of the condensation products is recovered. Indeed, during the condensation (step a ), a mixture of products is often obtained.
  • an oligomer A which is a mixture of isomers of formula where n1 and n2 are 0, 1 or 2 and n1 + n2 is less than or equal to 3.
  • MBT benzyltoluene
  • DBT dibenzyltoluene
  • oligomer B which is a mixture of isomers of formula: where n′1, n ⁇ 1 and n4 are 0, 1 or 2, n′2, n ⁇ 2, n3, n′3 and n5 are 0 or 1, and knowing that the sum n′1 + n ⁇ 1 + n′2 + n ⁇ 2 + n3 + n′3 + n4 + n5 is less than or equal to 2.
  • stage d the desired isomers or mixtures of isomers are distilled off, then they are conditioned into dielectric fluid.
  • the packaging of products for dielectric use is known per se, it is recalled on page 4 in patent application EP 8251. It consists of a preliminary purification treatment with alkalis such as NaoH, Na2Co3 or compounds similar to calcium or potassium at a temperature ranging from 20 to 350 ° C. Sometimes further distillation can be advantageous.
  • the next purification phase consists in using bleaching earth or activated alumina either alone or as a mixture according to the specific techniques known in the dielectric fluids sector.
  • stabilizers of the epoxide or other type such as, for example, tetraphenyltin or anthraquinone compounds.
  • aromatic halides are derived from the aromatic compounds in question, for example benzyl chloride and toluene or methyl benzyl chloride (CH3C6H4CH2Cl) and xylene, then it is possible to carry out upstream of the step to the partial halogenation of the aromatic compound. A mixture of aromatic halide and aromatic compound is thus obtained in which it suffices to add ferric chloride to carry out step a of the process.
  • oligomer A as described above which distills at 105-263 ° C under a vacuum of 15 mm of mercury.
  • the dielectric properties have been determined and are listed in the table of Example 7, column 7.1.
  • Example 3 is repeated, but replacing the ferric chloride with 35 g of aluminum chloride at the Friedel and Crafts reaction. The reaction medium is then subjected to distillation. The same difficulties are encountered as those observed in Example 2, which leads to a product unsuitable for dielectric application.
  • 1500 g are obtained under a vacuum of 15 mm of mercury vacuum with a vapor temperature of 260 to 280 ° C. It is a slightly yellow liquid containing less than 1 ppm of iron. This product is ideal for dielectric application.
  • the filtered samples were placed in tan ⁇ measuring cells (2 cells per sample). These cells were placed in an oven at 100 ° C and the tan ⁇ was followed for 500 hours.

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Spectroscopy & Molecular Physics (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Organic Insulating Materials (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)
  • Inorganic Insulating Materials (AREA)
  • Lubricants (AREA)
  • Compounds Of Iron (AREA)
  • Oxygen, Ozone, And Oxides In General (AREA)

Abstract

Simplification of the processes for the synthesis of dielectric fluids by condensation of aromatic halides and of aromatic compounds in the presence of ferric chloride. The Applicant has found that it is no longer necessary to neutralise the catalyst or to perform washings with aqueous solutions. <??>This avoids the generation of aqueous solutions contaminated with organic products, which it is difficult and costly to treat before they are discharged.

Description

La présente invention concerne un procédé de synthèse de fluides diélectriques et plus particulièrement un perfec­tionnement des procédés comprenant une condensation du type FRIEDEL et CRAFTS catalysée par le chlorure ferrique.The present invention relates to a process for the synthesis of dielectric fluids and more particularly to an improvement of the processes comprising a condensation of the FRIEDEL and CRAFTS type catalyzed by ferric chloride.

Dans la demande de brevet européen EP 8251, on a décrit des liquides diélectriques de formule

Figure imgb0001
dans laquelle n, x, y et z ont la valeur 1 ou 2. Ces produits peuvent être préparés par condensation de :
Figure imgb0002
dans lesquels n, x, y et z ont la même signification que ci-­dessus en présence d'un catalyseur de FRIEDEL et CRAFTS. Après la condensation, on procède à la destruction du catalyseur par exemple par addition d'une solution aqueuse diluée d'acide chlorhydrique suivie d'un lavage de la phase organique. La de­manderesse a découvert que si on utilise du chlorure ferrique comme catalyseur de FRIEDEL et CRAFTS, il n'est pas nécessaire de détruire le catalyseur et laver, c'est-à-dire qu'on obtient à l'issue du procédé de préparation, dans lequel on a omis l'étape de destruction et lavage du catalyseur, des liquides diélectriques ayant les mêmes propriétés que si on les avait préparés par le procédé conventionnel avec destruction et lavage.In European patent application EP 8251, dielectric liquids of the formula have been described
Figure imgb0001
in which n, x, y and z have the value 1 or 2. These products can be prepared by condensation of:
Figure imgb0002
in which n, x, y and z have the same meaning as above in the presence of a catalyst from FRIEDEL and CRAFTS. After the condensation, the catalyst is destroyed, for example by adding a dilute aqueous solution of hydrochloric acid followed by washing the organic phase. The Applicant has discovered that if ferric chloride is used as FRIEDEL and CRAFTS catalyst, it is not necessary to destroy the catalyst and wash, that is to say that one obtains at the end of the preparation process , in which the step of destruction and washing of the catalyst was omitted, dielectric liquids having the same properties as if they had been prepared by the conventional process with destruction and washing.

Par contre, si on utilise d'autres catalyseurs, par exemple du chlorure d'aluminium, on ne peut pas se passer de cette étape de destruction et lavage. En effet, si on omet cette étape, les produits obtenus sont inaptes à un usage comme fluide diélectrique. Cette découverte permet donc de ré­ soudre un important problème technique. En effet, la destruc­tion du catalyseur de condensation FRIEDEL et CRAFTS est faite, le plus souvent, par une solution aqueuse. On obtient donc une solution aqueuse contenant des produits organiques, et bien que la quantité de produits organiques soit faible, il est nécessaire de traiter cette solution aqueuse avant son rejet.On the other hand, if other catalysts are used, for example aluminum chloride, one cannot do without this destruction and washing step. Indeed, if this step is omitted, the products obtained are unsuitable for use as a dielectric fluid. This discovery therefore makes it possible to re solve a major technical problem. In fact, the destruction of the FRIEDEL and CRAFTS condensation catalyst is most often done with an aqueous solution. An aqueous solution containing organic products is therefore obtained, and although the quantity of organic products is small, it is necessary to treat this aqueous solution before its rejection.

La demande de brevet EP 136230 décrit des fluides di­électriques qui sont des oligomères de polyarylalcanes obtenus par condensation de chlorure de benzyle C₆H₅CH₂Cl et chlorure de benzylidène C₆H₅CHCl₂ sur le toluène en présence d'un cata­lyseur FRIEDEL et CRAFTS. La demanderesse a fait la même ob­servation que pour le procédé de la demande EP 8251 précédem­ment citée, c'est-à-dire qu'en utilisant le chlorure ferrique, on peut omettre l'étape du lavage et cependant produire un fluide apte à l'usage diélectrique.Patent application EP 136230 describes dielectric fluids which are polyarylalkane oligomers obtained by condensation of benzyl chloride C₆H₅CH₂Cl and benzylidene chloride C₆H₅CHCl₂ on toluene in the presence of a FRIEDEL and CRAFTS catalyst. The Applicant has made the same observation as for the process of the EP 8251 application cited above, that is to say that by using ferric chloride, it is possible to omit the washing step and yet produce a fluid capable of dielectric.

La demanderesse a trouvé un procédé particulièrement simple pour synthétiser des fluides diélectriques par une condensation de type FRIEDEL et CRAFTS.The Applicant has found a particularly simple process for synthesizing dielectric fluids by condensation of the FRIEDEL and CRAFTS type.

La présente invention est donc dans un procédé de syn­thèse de fluides diélectriques comprenant les étapes succes­sives suivantes :

  • a/ Condensation d'halogénures aromatiques et de compo­sés aromatiques en présence de chlorure ferrique comme cataly­seur
  • b/ Elimination du catalyseur par neutralisation ou la­vage ou toute combinaison de ces moyens
  • c/ Distillation éventuelle de l'excédent des réactifs
  • d/ Distillation de l'ensemble des produits de conden­sation ou d'au moins l'un d'entre eux suivie de son condition­nement en fluide diélectrique,le perfectionnement consistant à supprimer l'étape b.
The present invention is therefore in a process for the synthesis of dielectric fluids comprising the following successive steps:
  • a / Condensation of aromatic halides and aromatic compounds in the presence of ferric chloride as catalyst
  • b / Removal of the catalyst by neutralization or washing or any combination of these means
  • c / Possible distillation of excess reagents
  • d / Distillation of all of the condensation products or at least one of them followed by its conditioning in dielectric fluid, the improvement consisting in eliminating step b .

Le procédé des étapes a à d est connu, il est décrit, par exemple, dans la demande de brevet EP 8251. La condensa­tion de l'étape a est une réaction de FRIEDEL et CRAFTS.The process of steps a to d is known, it is described, for example, in patent application EP 8251. The condensation of step a is a reaction of FRIEDEL and CRAFTS.

Les halogénures aromatiques désignent, par exemple, des alkylbenzène ou (polyalkyl)benzène ayant au moins un halogène en position benzylique sur la chaîne alkyl, le noyau benzé­ nique pouvant, en plus des chaînes alkyl halogénées, être sub­stitué par des halogènes, des alkyls ayant jusqu'à trois atomes de carbone ou des groupements nitriles ou NO₂.Aromatic halides denote, for example, alkylbenzene or (polyalkyl) benzene having at least one halogen in the benzyl position on the alkyl chain, the benzated nucleus nique can, in addition to halogenated alkyl chains, be substituted by halogens, alkyls having up to three carbon atoms or nitrile or NO₂ groups.

Les chaînes alkyl qui portent au moins un halogène peu­vent être identiques ou différentes et comporter jusqu'à trois atomes de carbone.The alkyl chains which carry at least one halogen can be identical or different and contain up to three carbon atoms.

Ces halogénures aromatiques peuvent être par exemple les produits de formules :

Figure imgb0003
These aromatic halides can be, for example, the products of formulas:
Figure imgb0003

Les halogénures aromatiques précédents sont condenses avec des composés aromatiques. Ces composés aromatiques dési­gnent, par exemple, du benzène pouvant être substitué par un ou plusieurs groupements alkyls identiques ou différents et ayant jusqu'à 8 atomes de carbone, des halogènes ou des grou­pements nitriles ou NO₂.The foregoing aromatic halides are condensed with aromatic compounds. These aromatic compounds denote, for example, benzene which can be substituted by one or more identical or different alkyl groups and having up to 8 carbon atoms, halogens or nitrile or NO₂ groups.

Ces composés aromatiques peuvent être, par exemple, du benzène, du toluène, du xylène, des produits de formule :

Figure imgb0004
These aromatic compounds can be, for example, benzene, toluene, xylene, products of formula:
Figure imgb0004

La condensation de l'étape a a lieu en pratique à une température comprise entre 50°C et 150°C. La quantité de chlo­rure ferrique est comprise habituellement entre 50 ppm et 1% en poids de la masse réactionnelle.The condensation of the step takes place in practice at a temperature between 50 ° C and 150 ° C. The amount of ferric chloride is usually between 50 ppm and 1% by weight of the reaction mass.

On peut utiliser dans cette étape a un excédent de l'halogénure aromatique ou un excédent du composé aromatique. Selon les proportions des différents réactifs, on obtient des produits de condensation différents et qui sont eux mêmes des mélanges. Le plus souvent, il peut être nécessaire de distil­ler l'excédent des réactifs (étape c) car ces produits, même en mélange avec les produits de condensation n'ont pas de pro­priétés diélectriques ou ne peuvent pas être utilisés comme diélectriques à cause de leur trop grande volatilité.In this step , an excess of the aromatic halide or an excess of the aromatic compound can be used. Depending on the proportions of the different reactants, different condensation products are obtained, which are themselves mixtures. Most often, it may be necessary to distill the excess reagents (step c ) because these products, even in admixture with the condensation products do not have dielectric properties or cannot be used as dielectrics because of their too much volatility.

Dans l'étape d, on récupère l'ensemble ou au moins un des produits de condensation. En effet, au cours de la conden­sation (étape a), on obtient souvent un mélange de produits.In step d , all or at least one of the condensation products is recovered. Indeed, during the condensation (step a ), a mixture of products is often obtained.

Par exemple, quand on condense du chlorure de benzyle sur du toluène, on obtient un oligomère A qui est un mélange d'isomères de formule

Figure imgb0005
dans laquelle n₁ et n₂ valent 0, 1 ou 2 et n₁+n₂ est inférieur ou égal à 3.For example, when benzyl chloride is condensed on toluene, an oligomer A is obtained which is a mixture of isomers of formula
Figure imgb0005
where n₁ and n₂ are 0, 1 or 2 and n₁ + n₂ is less than or equal to 3.

Le mélange peut contenir le produit de condensation tel que n₁ et n₂ = 0 qu'on appelle benzyltoluène (MBT) et le produit dans lequel n₁+n₂ = 1 qu'on appelle dibenzyltoluène (DBT).The mixture can contain the condensation product such as n₁ and n₂ = 0 which is called benzyltoluene (MBT) and the product in which n₁ + n₂ = 1 which is called dibenzyltoluene (DBT).

Par exemple, quand on condense du chlorure de benzyli­dène C₆H₅CHCl₂ sur du toluène et du DBT, on obtient un oligo­mère B qui est un mélange d'isomères de formule :

Figure imgb0006
dans laquelle n′₁, n˝₁ et n₄ valent 0, 1 ou 2,
n′₂, n˝₂, n₃, n′₃ et n₅ valent 0 ou 1,
et sachant que la somme n′₁ +n˝₁+n′₂+n˝₂+n₃+n′₃+n₄+n₅ est infé­rieure ou égale à 2.For example, when condensing benzylidene chloride C₆H₅CHCl₂ on toluene and DBT, we obtain an oligomer B which is a mixture of isomers of formula:
Figure imgb0006
where n′₁, n˝₁ and n₄ are 0, 1 or 2,
n′₂, n˝₂, n₃, n′₃ and n₅ are 0 or 1,
and knowing that the sum n′₁ + n˝₁ + n′₂ + n˝₂ + n₃ + n′₃ + n₄ + n₅ is less than or equal to 2.

Quand on condense un mélange de C₆H₅CH₂Cl et C₆H₅ CHCl₂ sur du toluène, on obtient un mélange des oligomères A et B.When one condenses a mixture of C₆H₅CH₂Cl and C₆H₅ CHCl₂ on toluene, one obtains a mixture of oligomers A and B.

Dans l'étape d, on sépare par distillation les isomères ou les mélanges d'isomères souhaités, puis on les conditionne en fluide diélectrique. Le conditionnement des produits pour usage diélectrique est connu en soi, il est rappelé en page 4 dans la demande de brevet EP 8251. Il consiste en un traite­ment préliminaire de purification avec des alcalins tels que NaoH, Na₂Co₃ ou des composés analogues du calcium ou du po­tassium à une température pouvant aller de 20 à 350°C. Par­fois, une distillation ultérieure peut être avantageuse. Après ce traitement préliminaire, la phase de purification suivante consiste à employer une terre décolorante ou de l'alumine activée soit seules, soit en mélange selon les tech­niques spécifiques connues dans le secteur des fluides diélec­triques. De même, il peut être avantageux d'ajouter des stabi­lisants du type époxyde ou d'autre nature comme, par exemple, le tetraphenyletain ou des composés anthraquinoniques.In stage d , the desired isomers or mixtures of isomers are distilled off, then they are conditioned into dielectric fluid. The packaging of products for dielectric use is known per se, it is recalled on page 4 in patent application EP 8251. It consists of a preliminary purification treatment with alkalis such as NaoH, Na₂Co₃ or compounds similar to calcium or potassium at a temperature ranging from 20 to 350 ° C. Sometimes further distillation can be advantageous. After this preliminary treatment, the next purification phase consists in using bleaching earth or activated alumina either alone or as a mixture according to the specific techniques known in the dielectric fluids sector. Likewise, it may be advantageous to add stabilizers of the epoxide or other type, such as, for example, tetraphenyltin or anthraquinone compounds.

On ne sortirait pas du cadre de la présente invention en condensant dans l'étape a des mélanges d'halogénures aroma­tiques sur des mélanges de composés aromatiques.It would not be departing from the scope of the present invention to condense in step a mixtures of aromatic halides on mixtures of aromatic compounds.

Si les halogénures aromatiques dérivent des composés aromatiques en question, par exemple le chlorure de benzyle et le toluène ou le chlorure de méthyl benzyl (CH₃C₆H₄CH₂Cl) et le xylène, alors on peut effectuer en amont de l'étape a l'halogénation partielle du composé aromatique. On obtient ainsi un mélange d'halogénure aromatique et de composé aroma­tique dans lequel il suffit d'ajouter le chlorure ferrique pour effectuer l'étape a du procédé.If the aromatic halides are derived from the aromatic compounds in question, for example benzyl chloride and toluene or methyl benzyl chloride (CH₃C₆H₄CH₂Cl) and xylene, then it is possible to carry out upstream of the step to the partial halogenation of the aromatic compound. A mixture of aromatic halide and aromatic compound is thus obtained in which it suffices to add ferric chloride to carry out step a of the process.

EXEMPLE 1EXAMPLE 1

Dans un réacteur muni d'une agitation relative et d'un condenseur, on coule en 4 heures 6 moles de chlorure de ben­zyle dans 30 moles de toluène contenant 35 g de FeCl₃ à la température de 105°C. Après fin d'introduction du chlorure de benzyle, la masse réactionnelle est maintenue encore 1 h 30 à 105°C. L'ensemble est ensuite soumis à une distillation simple qui permet de séparer :
a) le toluène non réagi, sous un vide de 15 mm de mercure avec une température de pied de 105°C. Le toluène re­cueilli est incolore, avec une pureté supérieure à 99 % d'après l'analyse chromatographique et contient moins de 2 ppm de fer.
b) l'oligomère A comme décrit précédemment qui distille à 105-263°C sous un vide de 15 mm de mercure. Le produit ob­tenu (900 g) qui est légèrement jaune a la composition suivante : n₁ + n₂ = 0 75 % n₁ + n₂ = 1 21 % n₁ + n₂ = 2 4 %
In a reactor fitted with relative agitation and a condenser, 6 moles of benzyl chloride are poured in 4 hours into 30 moles of toluene containing 35 g of FeCl₃ at a temperature of 105 ° C. After the end of introduction of the benzyl chloride, the reaction mass is maintained for another 1 hour 30 minutes at 105 ° C. The whole is then subjected to a simple distillation which makes it possible to separate:
a) unreacted toluene, under a vacuum of 15 mm of mercury with a bottom temperature of 105 ° C. The toluene collected is colorless, with a purity greater than 99% according to the chromatographic analysis and contains less than 2 ppm of iron.
b) oligomer A as described above which distills at 105-263 ° C under a vacuum of 15 mm of mercury. The product obtained (900 g) which is slightly yellow has the following composition: n₁ + n₂ = 0 75% n₁ + n₂ = 1 21% n₁ + n₂ = 2 4%

Le composé n₁ + n₂ = 0 est constitué uniquement par un mélange d'isomères de benzyltoluène dans la proportion 0/m/p = 42,7/6,6/50,7.The compound n₁ + n₂ = 0 consists only of a mixture of benzyltoluene isomers in the proportion 0 / m / p = 42.7 / 6.6 / 50.7.

Les propriétés diélectriques ont été déterminées et fi­gurent dans le tableau de l'exemple 7, colonne 7.1.The dielectric properties have been determined and are listed in the table of Example 7, column 7.1.

Un produit obtenu de la même manière, mais en effec­tuant les lavages suivants sur la phase organique en fin de réaction du chlorure de benzyle :
2 X 1000 cc d'acide chlorhydrique 3 %
3 X 1000 cc d'eau
conduit à un produit dont les propriétés figurent dans le ta­ conduit à un produit dont les propriétés figurent dans le ta­bleau de l'exemple 7, colonne 7.2.
A product obtained in the same way, but by carrying out the following washes on the organic phase at the end of the reaction of the benzyl chloride:
2 X 1000 cc of 3% hydrochloric acid
3 X 1000 cc of water
leads to a product whose properties are listed in the ta leads to a product whose properties are shown in the table in Example 7, column 7.2.

On constate qu'il n'y a aucune différence dans les pro­priétés diélectriques.It can be seen that there is no difference in the dielectric properties.

EXEMPLE 2 (non conforme à l'invention) EXAMPLE 2 (not in accordance with the invention)

On réalise la même opération de condensation du chlo­rure de benzyle sur le toluène que dans l'exemple 1, mais en remplaçant le chlorure ferrique par 35 g de chlorure d'aluminium. Le milieu réactionnel en fin de réaction du chlo­rure de benzyle est soumis à une distillation simple comme dans l'exemple 1 ce qui conduit aux produits suivants :

  • a) le toluène non réagi sous un vide de 15 mm de mer­cure avec une température de pied de 105°C. Ce toluène est jaune et contient 3,2 ppm d'aluminium. L'analyse chromatogra­phique montre que ce toluène est très impur et contient notam­ment des quantités non négligeables de benzène et de xylène ;
  • b) la distillation des produits plus lourds est pour­suivie en augmentant progressivement la température avec un vide plus poussé. Cette distillation est très difficile car il y a décomposition permanente avec formation de benzène, to­luène et xylène avec des difficultés pour obtenir le vide.
The same operation of condensing benzyl chloride on toluene is carried out as in Example 1, but replacing the ferric chloride with 35 g of aluminum chloride. The reaction medium at the end of the reaction of the benzyl chloride is subjected to a simple distillation as in Example 1, which leads to the following products:
  • a) unreacted toluene under a vacuum of 15 mm of mercury with a bottom temperature of 105 ° C. This toluene is yellow and contains 3.2 ppm of aluminum. Chromatographic analysis shows that this toluene is very impure and contains in particular non-negligible quantities of benzene and xylene;
  • b) the distillation of heavier products is continued by gradually increasing the temperature with a higher vacuum. This distillation is very difficult because there is permanent decomposition with the formation of benzene, toluene and xylene with difficulties in obtaining the vacuum.

On obtient seulement 300 g de produit très fortement coloré contenant 17 ppm d'aluminium ayant la composition suivante : benzène 1,3 % toluène 16,0 % xylène 7,0 % diphénylméthane 7,5 % benzyltoluène 34,0 % benzylxylène 22,0 % Only 300 g of very strongly colored product containing 17 ppm of aluminum having the following composition are obtained: benzene 1.3% toluene 16.0% xylene 7.0% diphenylmethane 7.5% benzyltoluene 34.0% benzylxylene 22.0%

Ce produit est évidemment inutilisable dans l'application diélectrique. Par ailleurs il reste une quantité très importante de produit dans le ballon de distillation sous forme d'un bloc compact irrécupérable.This product is obviously unusable in the dielectric application. In addition, a very large quantity of product remains in the distillation flask in the form of an irretrievable compact block.

En conclusion, un produit brut de benzylation du to­ luène catalysée par le chlorure d'aluminium n'est pas distil­lable sans un lavage préalable permettant d'éliminer le cata­lyseur.In conclusion, a gross benzylation product of to luene catalyzed by aluminum chloride is not distillable without a preliminary washing making it possible to remove the catalyst.

EXEMPLE 3EXAMPLE 3

On opère comme dans l'exemple 1 du brevet, sauf qu'au lieu d'utiliser du chlorure de benzyle pur, on utilise un pro­duit brut de photochloration du toluène. Pour cela, on intro­duit 6 moles de chlore dans 24 moles de toluène sous irradia­tion photochimique à la température de 90°C. Le produit de la réaction est introduit progressivement dans 12 moles de to­luène contenant 35 g de FeCl₃ à 105°C. Après fin de réaction, le milieu est distillé comme dans l'exemple 1 permettant de séparer :

  • a) le toluène non réagi avec une pureté supérieure à 99 %, directement utilisable dans une nouvelle opération de synthèse ;
  • b) un mélange d'oligomère A et d'oligomère B comme dé­crit précédemment dans la proportion pondérale 97,5/2,5.
The procedure is as in Example 1 of the patent, except that instead of using pure benzyl chloride, a crude product of photochlorination of toluene is used. For this, 6 moles of chlorine are introduced into 24 moles of toluene under photochemical irradiation at a temperature of 90 ° C. The reaction product is gradually introduced into 12 moles of toluene containing 35 g of FeCl₃ at 105 ° C. After the end of the reaction, the medium is distilled as in Example 1, making it possible to separate:
  • a) unreacted toluene with a purity greater than 99%, directly usable in a new synthesis operation;
  • b) a mixture of oligomer A and oligomer B as described above in the weight proportion 97.5 / 2.5.

Les propriétés diélectriques ont été déterminées et fi­gurent dans le tableau de l'exemple 7, colonne 7.3.The dielectric properties have been determined and appear in the table of Example 7, column 7.3.

Un produit obtenu de la même manière mais en effectuant des lavages à l'acide chlorhydrique aqueux et à l'eau sur la phase organique après la fin de réaction de Friedel et Crafts conduit à un produit dont les propriétés diélectriques figu­rent dans le tableau de l'exemple 7, colonne 7.4. On constate bien qu'il n'y a aucune différence dans les propriétés diélec­triques.A product obtained in the same way but by washing with hydrochloric acid and water on the organic phase after the end of the Friedel and Crafts reaction leads to a product whose dielectric properties are shown in the table of l 'example 7, column 7.4. It can be seen that there is no difference in the dielectric properties.

EXEMPLE 4EXAMPLE 4

On reproduit l'exemple 3 mais en remplaçant le chlorure ferrique par 35 g de chlorure d'aluminium à la réaction de Friedel et Crafts. Le milieu réactionnel est ensuite soumis à la distillation. Les mêmes difficultés sont rencontrées que celles observées dans l'exemple 2, ce qui conduit à un produit impropre pour l'application diélectrique.Example 3 is repeated, but replacing the ferric chloride with 35 g of aluminum chloride at the Friedel and Crafts reaction. The reaction medium is then subjected to distillation. The same difficulties are encountered as those observed in Example 2, which leads to a product unsuitable for dielectric application.

EXEMPLE 5EXAMPLE 5

On opère comme dans l'exemple 3 du brevet, sauf que l'on utilise un mélange d'isomères de dichlorotoluènes (33 % de 2-4, 26,5 % de 2-5, 18,8 % de 2-6, 11,6 % de 2-3, 8,1 % de 3-4). On effectue la réaction photochimique de 6 moles de chlore avec 24 moles de dichlorotoluènes à 120°C. On effectue ensuite la réaction de Friedel et Crafts en faisant réagir le milieu réactionnel de photochloration avec 12 moles de dichlo­rotoluènes en présence de 20 g de FeCl₃ à la température de 140°C. L'introduction s'effectue en 4 h 30 avec ajout régulier de petites quantités de FeCl₃. La masse réactionnelle est conservée encore 1 h 30 sous agitation à 140°C, puis soumise à une distillation simple sous vide qui permet de séparer :

  • a) les dichlorotoluènes non réagis, sous un vide de 15 mm de mercure avec une température de pied de 150°C. Le distillat obtenu est incolore et contient moins de 1 ppm de fer. L'analyse chromatographique montre que la teneur en di­chlorotoluènes est supérieure à 99 % ;
  • b) les produits de formule :
    Figure imgb0007
The procedure is as in Example 3 of the patent, except that a mixture of dichlorotoluene isomers (33% of 2-4, 26.5% of 2-5, 18.8% of 2-6, 11.6% of 2-3, 8.1% of 3-4). The photochemical reaction of 6 moles of chlorine is carried out with 24 moles of dichlorotoluenes at 120 ° C. The Friedel and Crafts reaction is then carried out by reacting the photochlorination reaction medium with 12 moles of dichlorotoluenes in the presence of 20 g of FeCl₃ at a temperature of 140 ° C. The introduction takes place in 4 h 30 with regular addition of small amounts of FeCl₃. The reaction mass is kept for another 1 h 30 with stirring at 140 ° C., then subjected to simple distillation under vacuum which makes it possible to separate:
  • a) unreacted dichlorotoluenes, under a vacuum of 15 mm of mercury with a bottom temperature of 150 ° C. The distillate obtained is colorless and contains less than 1 ppm of iron. Chromatographic analysis shows that the dichlorotoluene content is greater than 99%;
  • b) the products of formula:
    Figure imgb0007

1500 g sont obtenus sous un vide de 15 mm de mercure de vide avec une température de vapeur de 260 à 280°C. C'est un liquide légèrement jaune contenant moins de 1 ppm de fer. Ce produit convient parfaitement pour l'application diélectrique.1500 g are obtained under a vacuum of 15 mm of mercury vacuum with a vapor temperature of 260 to 280 ° C. It is a slightly yellow liquid containing less than 1 ppm of iron. This product is ideal for dielectric application.

Un produit obtenu de la même manière mais avec lavages de la phase organique issue de la réaction de Friedel et Crafts par de l'acide chlorhydrique aqueux et ensuite à l'eau conduit à un produit identique à celui obtenu sans lavage du catalyseur.A product obtained in the same way but with washing of the organic phase resulting from the Friedel and Crafts reaction with aqueous hydrochloric acid and then with water leads to a product identical to that obtained without washing the catalyst.

On a mesuré les propriétés diélectriques de ces deux produits (avec lavage et sans lavage) comme dans l'exemple 7, il n'y a aucune différence, les deux produits conviennent comme diélectrique.The dielectric properties of these two products were measured (with washing and without washing) as in Example 7, there is no difference, the two products are suitable as dielectric.

EXEMPLE 6 (non conforme à l'invention) EXAMPLE 6 (not in accordance with the invention)

On reproduit l'exemple 5 mais en remplaçant le chlorure ferrique par 35 g de chlorure d'aluminium. Le produit après fin de réaction de Friedel et Crafts est soumis à une distil­lation simple pour séparer :

  • a) les dichlorotoluènes non réagis sous vide de 15 mm de mercure avec une température de pied de 150°C. La distilla­tion est très difficile à conduire à cause de la formation de mousses dues à des réactions de décomposition. Les dichloroto­luènes obtenus sont très colorés et contiennent 95 ppm d'aluminium. La pureté d'après l'analyse CPG est de 85 % seu­lement (contiennent 10 % de produits légers et 5 % de produits lourds).
  • b) les produits plus lourds : en augmentant progressi­vement la température pour atteindre 240-280°C, il y a des dépôts blanchâtres, le distillat très coloré s'épaissit on n'obtient que 1200 g du produit contenant au moins 10 % de plus légers (dichlorobenzènes et dichlorotoluènes générées par décomposition) et 170 ppm d'aluminium.
Example 5 is reproduced, but replacing the ferric chloride with 35 g of aluminum chloride. The product after the end of the Friedel and Crafts reaction is subjected to a simple distillation to separate:
  • a) the unreacted dichlorotoluenes under vacuum of 15 mm of mercury with a bottom temperature of 150 ° C. Distillation is very difficult to conduct due to the formation of foams due to decomposition reactions. The dichlorotoluenes obtained are very colored and contain 95 ppm of aluminum. The purity according to the CPG analysis is only 85% (contains 10% of light products and 5% of heavy products).
  • b) heavier products : gradually increasing the temperature to reach 240-280 ° C, there are whitish deposits, the very colored distillate thickens, only 1200 g of the product containing at least 10% more are obtained light (dichlorobenzenes and dichlorotoluenes generated by decomposition) and 170 ppm of aluminum.

Ce produit bien évidement est impropre à une utilisa­tion comme diélectrique.This product is obviously unsuitable for use as a dielectric.

Il ne reste au fond du ballon une quantité importante de produit sous forme de bloc compact noir irrécupérable.There is only a large quantity of product left in the bottom of the flask in the form of an irretrievable black compact block.

En conclusion, on ne peut obtenir les produits souhai­tés sans un lavage préalable du milieu réactionnel pour élimi­ner le chlorure d'aluminium.In conclusion, the desired products cannot be obtained without a prior washing of the reaction medium to remove the aluminum chloride.

EXEMPLE 7 : Propriétés diélectriques EXAMPLE 7 Dielectric properties

Elles sont mesurées par des essais de vieillissement en cellule à 100°C.They are measured by cell aging tests at 100 ° C.

Les échantillons ont été traités une nuit à température ambiante par 3 % de TONSIL 13 activé, après ajout de 1 % d'époxyde DGEBA (diglycidil éther du bisphénol A).The samples were treated overnight at room temperature with 3% of activated TONSIL 13, after addition of 1% of DGEBA epoxy (diglycidil ether of bisphenol A).

Les échantillons filtrés ont été mis dans des cellules de mesure de tanδ (2 cellules par échantillons). Ces cellules ont été placées dans une étuve à 100°C et la tanδ a été suivie pendant 500 heures.The filtered samples were placed in tanδ measuring cells (2 cells per sample). These cells were placed in an oven at 100 ° C and the tanδ was followed for 500 hours.

Les résultats obtenus, donnés dans le tableau ci-après, montrent que les quatre produits ont une stabilité équiva­lente. tanδ x 10⁻⁴ (100°C) 7.1 7.2 7.3 7.4 Temps 1 2 1 2 1 2 1 2 0 1,4 2,1 2,0 1,7 1,9 1,9 1,6 2,1 30′ 1,2 1,9 1,9 1,5 1,8 1,7 1,5 1,9 18 h 1,5 1,8 1,9 1,7 1,7 1,7 1,6 1,8 41 h 1,8 2,4 2,1 2,0 2,0 2,2 1,9 2,3 140 h 2,3 2,7 2,0 2,4 3,0 1,9 2,4 2,9 210 h 2,4 3,0 2,5 2,7 2,9 3,0 2,8 3,0 260 h 2,6 3,3 3,0 3,5 3,6 5,0 3,1 4,2 310 h 3,4 3,9 4,1 4,0 4,9 5,5 3,9 5,0 370 h 4,2 5,0 4,6 4,9 5,5 5,7 4,8 5,9 440 h 5,6 6,0 6,1 5,9 6,5 6,0 5,9 6,6 510 h Arrêt 9,3 10,6 9,0 10,9 8,5 9,6 7,7 11,0 The results obtained, given in the table below, show that the four products have equivalent stability. tanδ x 10⁻⁴ (100 ° C) 7.1 7.2 7.3 7.4 Time 1 2 1 2 1 2 1 2 0 1.4 2.1 2.0 1.7 1.9 1.9 1.6 2.1 30' 1.2 1.9 1.9 1.5 1.8 1.7 1.5 1.9 6 p.m. 1.5 1.8 1.9 1.7 1.7 1.7 1.6 1.8 41 h 1.8 2.4 2.1 2.0 2.0 2.2 1.9 2.3 140 hrs 2.3 2.7 2.0 2.4 3.0 1.9 2.4 2.9 210 h 2.4 3.0 2.5 2.7 2.9 3.0 2.8 3.0 260 h 2.6 3.3 3.0 3.5 3.6 5.0 3.1 4.2 310 h 3.4 3.9 4.1 4.0 4.9 5.5 3.9 5.0 370 h 4.2 5.0 4.6 4.9 5.5 5.7 4.8 5.9 440 h 5.6 6.0 6.1 5.9 6.5 6.0 5.9 6.6 510 h Stop 9.3 10.6 9.0 10.9 8.5 9.6 7.7 11.0

Claims (4)

1. Dans un procédé de synthèse de fluides diélectriques comprenant les étapes successives suivantes : a/ condensation d'halogénures aromatiques et de compo­sés aromatiques en présence de chlorure ferrique, comme cata­lyseur, b/ élimination du catalyseur par neutralisation ou la­vage ou toute combinaison de ces moyens, c/ distillation éventuelle de l'excédent des réactifs, d/ distillation de l'ensemble des produits de condensa­tion ou d'au moins l'un d'entre eux suivie de son conditionne­ment en fluide diélectrique, le perfectionnement consistant à supprimer l'étape b. 1. In a process for the synthesis of dielectric fluids comprising the following successive steps: a / condensation of aromatic halides and aromatic compounds in the presence of ferric chloride, as catalyst, b / elimination of the catalyst by neutralization or washing or any combination of these means, c / possible distillation of the excess reagents, d / distillation of all of the condensation products or of at least one of them followed by its conditioning in dielectric fluid, the improvement consisting in eliminating step b . 2. Procédé selon la revendication 1 caractérisé en ce que l'halogénure aromatique est du chlorure de benzyle et que le composé aromatique est du toluène. 2. Method according to claim 1 characterized in that the aromatic halide is benzyl chloride and that the aromatic compound is toluene. 3. Procédé selon la revendication 2 caractérisé en ce que l'halogénure aromatique est un mélange de chlorure de ben­zyle (C₆H₅CH₂Cl) et de chlorure de benzylidène (C₆H₅CHCl₂). 3. Method according to claim 2 characterized in that the aromatic halide is a mixture of benzyl chloride (C₆H₅CH₂Cl) and benzylidene chloride (C₆H₅CHCl₂). 4. Procédé selon la revendication 1 caractérisé en ce que l'halogénure aromatique est un produit de formule
Figure imgb0008
et que le composé aromatique est du dichlorotoluène
Figure imgb0009
4. Method according to claim 1 characterized in that the aromatic halide is a product of formula
Figure imgb0008
and that the aromatic compound is dichlorotoluene
Figure imgb0009
EP90402722A 1989-10-13 1990-10-02 Process for the preparation of dielectric fluids Expired - Lifetime EP0422986B1 (en)

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FR931987A (en) * 1945-08-17 1948-03-09 Solar Mfg Corp Method of manufacturing a dielectric based on toluene and its homologues
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FR2510135A1 (en) * 1981-07-24 1983-01-28 Ugine Kuhlmann DIELECTRIC FLUID FOR TRANSFORMERS AND PROCESS FOR PREPARING THE SAME
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FR931987A (en) * 1945-08-17 1948-03-09 Solar Mfg Corp Method of manufacturing a dielectric based on toluene and its homologues
BE533352A (en) * 1953-11-17 1954-12-15
FR2510135A1 (en) * 1981-07-24 1983-01-28 Ugine Kuhlmann DIELECTRIC FLUID FOR TRANSFORMERS AND PROCESS FOR PREPARING THE SAME
EP0136230A1 (en) * 1983-09-23 1985-04-03 Elf Atochem S.A. Compositions of oligomers of polyaryl alkanes, and process for their preparation

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