EP0422986A1 - Process for the preparation of dielectric fluids - Google Patents
Process for the preparation of dielectric fluids Download PDFInfo
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- 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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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01B—CABLES; CONDUCTORS; INSULATORS; SELECTION OF MATERIALS FOR THEIR CONDUCTIVE, INSULATING OR DIELECTRIC PROPERTIES
- H01B3/00—Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties
- H01B3/18—Insulators or insulating bodies characterised by the insulating materials; Selection of materials for their insulating or dielectric properties mainly consisting of organic substances
- H01B3/20—Insulators 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
- H01B3/22—Insulators 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
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M105/00—Lubricating compositions characterised by the base-material being a non-macromolecular organic compound
- C10M105/02—Well-defined hydrocarbons
- C10M105/06—Well-defined hydrocarbons aromatic
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M105/00—Lubricating compositions characterised by the base-material being a non-macromolecular organic compound
- C10M105/50—Lubricating compositions characterised by the base-material being a non-macromolecular organic compound containing halogen
- C10M105/52—Lubricating compositions characterised by the base-material being a non-macromolecular organic compound containing halogen containing carbon, hydrogen and halogen only
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2203/00—Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
- C10M2203/06—Well-defined aromatic compounds
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2211/00—Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions
- C10M2211/02—Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions containing carbon, hydrogen and halogen only
- C10M2211/024—Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions containing carbon, hydrogen and halogen only aromatic
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2211/00—Organic non-macromolecular compounds containing halogen as ingredients in lubricant compositions
- C10M2211/06—Perfluorinated compounds
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/14—Electric or magnetic purposes
- C10N2040/16—Dielectric; Insulating oil or insulators
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10N—INDEXING SCHEME ASSOCIATED WITH SUBCLASS C10M RELATING TO LUBRICATING COMPOSITIONS
- C10N2040/00—Specified use or application for which the lubricating composition is intended
- C10N2040/14—Electric or magnetic purposes
- C10N2040/17—Electric 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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- 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
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
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.
- 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 :
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 :
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
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 :
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:
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.
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 :
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:
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.
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.
- 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 :
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.
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.
- 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.
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.
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 :
- 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:
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.
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.
- 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.
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.
Claims (4)
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AT90402722T ATE80176T1 (en) | 1989-10-13 | 1990-10-02 | PROCESS FOR THE PRODUCTION OF DIELECTRIC LIQUIDS. |
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FR8913451A FR2653134B1 (en) | 1989-10-13 | 1989-10-13 | PROCESS FOR THE SYNTHESIS OF DIELECTRIC FLUIDS. |
FR8913451 | 1989-10-13 |
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US (1) | US5186864A (en) |
EP (1) | EP0422986B1 (en) |
JP (1) | JP2569214B2 (en) |
KR (1) | KR930005531B1 (en) |
CN (1) | CN1029005C (en) |
AT (1) | ATE80176T1 (en) |
CA (1) | CA2027445C (en) |
DE (1) | DE69000288T2 (en) |
DK (1) | DK0422986T3 (en) |
ES (1) | ES2034844T3 (en) |
FI (1) | FI97478C (en) |
FR (1) | FR2653134B1 (en) |
GR (1) | GR3006387T3 (en) |
IE (1) | IE64608B1 (en) |
NO (1) | NO904393L (en) |
PT (1) | PT95588B (en) |
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US5977422A (en) * | 1997-06-09 | 1999-11-02 | The Dow Chemical Company | Organoaluminum catalysis of alkylation reactions |
US20060100466A1 (en) * | 2004-11-08 | 2006-05-11 | Holmes Steven A | Cycloalkane base oils, cycloalkane-base dielectric liquids made using cycloalkane base oils, and methods of making same |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
Family Cites Families (5)
Publication number | Priority date | Publication date | Assignee | Title |
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US2012302A (en) * | 1933-04-04 | 1935-08-27 | Gen Electric | Halogenated material and process of preparing the same |
US3006972A (en) * | 1959-08-21 | 1961-10-31 | Standard Oil Co | Coupling of aromatic rings |
US4197417A (en) * | 1977-09-28 | 1980-04-08 | Imperial Chemical Industries Limited | Process for the manufacture of o-benzyl toluenes |
DE2962136D1 (en) * | 1978-07-27 | 1982-03-25 | Ugine Kuhlmann | Dielectric liquids, manufacturing process and uses |
DE3836780A1 (en) * | 1988-10-28 | 1990-05-03 | Bayer Ag | METHOD FOR PRODUCING OPTIONALLY SUBSTITUTED BENZYLBENZENE |
-
1989
- 1989-10-13 FR FR8913451A patent/FR2653134B1/en not_active Expired - Lifetime
-
1990
- 1990-10-02 ES ES199090402722T patent/ES2034844T3/en not_active Expired - Lifetime
- 1990-10-02 AT AT90402722T patent/ATE80176T1/en active
- 1990-10-02 EP EP90402722A patent/EP0422986B1/en not_active Expired - Lifetime
- 1990-10-02 DK DK90402722.4T patent/DK0422986T3/en active
- 1990-10-02 DE DE9090402722T patent/DE69000288T2/en not_active Expired - Fee Related
- 1990-10-11 NO NO90904393A patent/NO904393L/en unknown
- 1990-10-12 KR KR1019900016202A patent/KR930005531B1/en not_active IP Right Cessation
- 1990-10-12 CA CA002027445A patent/CA2027445C/en not_active Expired - Fee Related
- 1990-10-12 PT PT95588A patent/PT95588B/en not_active IP Right Cessation
- 1990-10-12 FI FI905033A patent/FI97478C/en not_active IP Right Cessation
- 1990-10-12 JP JP2275155A patent/JP2569214B2/en not_active Expired - Lifetime
- 1990-10-13 CN CN90108455A patent/CN1029005C/en not_active Expired - Fee Related
- 1990-10-15 US US07/597,030 patent/US5186864A/en not_active Expired - Fee Related
- 1990-10-15 IE IE369290A patent/IE64608B1/en not_active IP Right Cessation
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Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
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 |
Non-Patent Citations (1)
Title |
---|
DATABASE WPI, no. 74-20301V, Derwent Publications Ltd, Londres, GB; & JP-A-48 095 599 (KANEGAFUCHI CHEM. IND. CO.) 07-12-1973 * |
Also Published As
Publication number | Publication date |
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PT95588B (en) | 1997-08-29 |
ES2034844T3 (en) | 1993-04-01 |
DE69000288D1 (en) | 1992-10-08 |
EP0422986B1 (en) | 1992-09-02 |
CA2027445A1 (en) | 1991-04-14 |
DK0422986T3 (en) | 1992-10-05 |
FI905033A0 (en) | 1990-10-12 |
FI97478C (en) | 1996-12-27 |
JP2569214B2 (en) | 1997-01-08 |
KR910008113A (en) | 1991-05-30 |
KR930005531B1 (en) | 1993-06-22 |
DE69000288T2 (en) | 1993-03-18 |
IE64608B1 (en) | 1995-08-23 |
IE903692A1 (en) | 1991-04-24 |
US5186864A (en) | 1993-02-16 |
CA2027445C (en) | 1994-03-22 |
ATE80176T1 (en) | 1992-09-15 |
NO904393D0 (en) | 1990-10-11 |
FI97478B (en) | 1996-09-13 |
CN1029005C (en) | 1995-06-21 |
FR2653134B1 (en) | 1991-12-13 |
FR2653134A1 (en) | 1991-04-19 |
JPH03134095A (en) | 1991-06-07 |
GR3006387T3 (en) | 1993-06-21 |
PT95588A (en) | 1991-09-13 |
NO904393L (en) | 1991-04-15 |
CN1050894A (en) | 1991-04-24 |
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