WO2001002446A1 - Catalytic system based on rare earth and magnesium. novel neodymium alcoholate, use for polymerising unsaturated compounds - Google Patents
Catalytic system based on rare earth and magnesium. novel neodymium alcoholate, use for polymerising unsaturated compounds Download PDFInfo
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- WO2001002446A1 WO2001002446A1 PCT/FR2000/001863 FR0001863W WO0102446A1 WO 2001002446 A1 WO2001002446 A1 WO 2001002446A1 FR 0001863 W FR0001863 W FR 0001863W WO 0102446 A1 WO0102446 A1 WO 0102446A1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/0201—Oxygen-containing compounds
- B01J31/0211—Oxygen-containing compounds with a metal-oxygen link
- B01J31/0212—Alkoxylates
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/10—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of rare earths
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/02—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
- B01J31/12—Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing organo-metallic compounds or metal hydrides
- B01J31/122—Metal aryl or alkyl compounds
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/28—Metal alcoholates
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F10/02—Ethene
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/52—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides selected from boron, aluminium, gallium, indium, thallium or rare earths
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F210/00—Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F210/02—Ethene
Definitions
- the present invention relates to a catalytic system based on rare earth and magnesium, a new neodymium alcoholate and their use for the polymerization of unsaturated compounds.
- the object of the invention is therefore the development of an efficient and simple preparation catalytic system
- the catalytic system according to the invention is characterized in that it comprises a compound constituted by the product of the reaction between
- the system of the invention is efficient and allows, according to preferred embodiments, to obtain unimodal polymers, if necessary homodispersed and with a high rate of syndiotacticity.
- the term “rare earth” is understood to mean the elements of the group constituted by ytt ⁇ um and the elements of the periodic classification with atomic number included inclusively between 57 and 71
- the catalytic system of the invention comprises a compound consisting of the product of the reaction of two reagents which will be described more precisely below
- the first reagent is a rare earth alcoholate.
- alcoholate is meant the products corresponding to the general formula (1) (TR) x (OR 1 ) y (X) z (S) t in which R 1 denotes an organic group, X a halogen and S a coordinating solvent and where x> 1, y> 1, z> 0 and t> 0.
- alcoholate also applies, in the context of the present invention, to alcoholates of formula (1) comprising several different radicals R 1 .
- the rare earth of the alcoholate can be more particularly yttrium, lanthanum, cerium, neodymium or samarium. Neodymium is preferred.
- the alcoholate is more particularly an alcoholate of an alcohol or of a polyol derived from an aliphatic or cyclic hydrocarbon and in particular from an aliphatic hydrocarbon, linear or branched, in more particularly in C 4 -C 8 . Mention may very particularly be made of tertiary alcoholates or polyalcoholates, for example tert-butylate or tertioamylate.
- the alcoholate can also be a phenate, that is to say a derivative of a compound of phenolic or polyphenolic type. According to a preferred embodiment of the invention, the alcoholate is prepared by specific methods which will be described more precisely below.
- a first method implements a reaction of a rare earth halide with an alkali or alkaline earth alcoholate.
- the halide can more particularly be a chloride and the alkali can be in particular sodium and potassium.
- the reaction is carried out in an anhydrous solvent medium and protected from air.
- the solvent medium is constituted by tetrahydrofuran (THF) or comprises tetrahydrofuran in mixture with another solvent.
- THF tetrahydrofuran
- solvent mention may be made of liquid hydrocarbons of 3 to 12 carbon atoms such as heptane, cyclohexane, cyclic or aromatic hydrocarbons such as benzene, toluene or even xylenes.
- ethers are examples of ethers.
- the reaction generally takes place at a temperature which can be between ambient (20 ° C.) and 100 ° C. over a period which can vary between approximately 12 hours and approximately 96 hours.
- a temperature which can be between ambient (20 ° C.) and 100 ° C. over a period which can vary between approximately 12 hours and approximately 96 hours.
- the reaction mixture is brought to reflux over a period of the same order of magnitude.
- the reaction medium is allowed to settle, the supernatant is evaporated and a solid product is thus obtained, in the form of a powder, which constitutes the rare earth alcoholate.
- a second specific process consists in reacting with an alkali or alkaline earth alcoholate an adduct of a rare earth halide and THF (TRX 3 , xTHF).
- the adduct can be obtained by heating a rare earth halide in THF, for example at 50 ° C., then evaporation of the solvent. This evaporation can be done under vacuum at 20 ° C.
- the reaction with the alcoholate also takes place in an anhydrous solvent medium and away from air. and under the same conditions as those described for the previous process
- the solvents are of the same type as those given above and mention may be made very particularly of toluene
- This process consists in reacting an alcohol with a rare earth amide.
- the alcohol can be an alcohol, a polyol or a phenolic or polyphenolic compound as defined above.
- the amide is a compound. of formula TR (N (S ⁇ R 2 3 ) 2 ) 3 , R 2 denoting an alkyl radical, for example methyl
- the reaction is also carried out in an anhydrous solvent medium and protected from air
- the solvent medium consists of tetrahydrofuran (THF) or comprises tetrahydrofuran in admixture with another solvent.
- liquid hydrocarbons of 3 to 12 carbon atoms such as heptane, cyclohexane, cyclic or aromatic hydrocarbons such as benzene, toluene or xylenes can also be mentioned ethers
- the reaction temperature can be between -20 ° C and 100 ° C, but generally one works at room temperature
- the reaction time can be short t vary between 15 minutes and 96 hours, it can be for example 24 hours
- the present invention also relates, as a new product, to a neodymium alcoholate.
- This neodymium alcoholate has as specific characteristic the fact that it does not contain chlorine in its structure.
- the known rare earth alcoholates by their mode of preparation, present either chlorine which belongs to their atomic structure even, or a liganded solvent, or both at the same time
- the alcoholate is a tert-butylate or a tertioamylate
- the neodymium alcoholate of the invention can correspond to the formula Nd 3 ( ⁇ 3-O t Bu) 2 ( ⁇ 2 -O t Bu) 3 ( ⁇ - O t Bu) 4 (THF) 2 nTHF or Nd 3 ( ⁇ 3 -O t Am ) 2 ( ⁇ 2 -O t Am) 3 ( ⁇ -O t Am) 4 (THF) 2 nTHF, where n can be 0 or 1
- the absence of chlorine can be demonstrated by X-ray analysis.
- the neodymium alcoholate of the invention can be prepared by implementing the specific methods which have been described above, in particular using tert-butylate or a tertioamylate or else the tertiobutanol or tertiobutyl alcohol
- the second reagent used in the reaction, the product of which constitutes the compound of the catalytic system of the invention, is an organomagnesium
- organo-magnesium is meant a product which is either a dialkyl-magnesian or a G ⁇ gnard reagent
- a dialkyl-magnesian that is to say the compounds of formula (2)
- R-Mg-R ' where R and R' denote alkyl radicals
- R and R ' may more particularly be n-hexyl Mention may also be made more particularly of the product of formula (2) in which R and R' are respectively butyl and ethyl
- the alkyl radicals R and / or R 'can also carry a heteroatom such as Si Mention may in particular be made of the radical -CH 2 -S ⁇ (CH 3 ) 3
- the organomagnesium can also be a G ⁇ gnard reagent, that is to say a compound of formula (3) R-Mg-X in which X denotes a halogen, the halogen can be bromine, chlorine or iodine, but use is more particularly made of those for which the halogen is bromine
- R may be any R may in particular be a saturated or non-ahcyclic or aromatic aliphatic radical R may more particularly be an alkyl radical, such as the ethyl radical, another phenyl radical
- the rare earth alcoholate and the magnesium compound can be reacted in respective variable proportions
- This proportion can be expressed by the ratio TR / Mg
- This ratio (molar ratio) is generally between 0.5 and 5 It can be more particularly equal to 1 It would not, however, depart from the scope of the present invention to use a ratio outside the above-mentioned range. This ratio may vary in particular as a function of the unsaturated compounds which it is desired to polymerize. It will be noted that the use of 'an organo-magnesian of formula (2) above in which R and R' are respectively butyl and ethyl makes it possible to work with TR / Mg ratios which can vary within a fairly wide range
- the product of the reaction of the two reactants which have just been described therefore constitutes the compound of the catalytic system of the invention.
- consists of the product of the reaction of the two reactants it is meant that there is no other compounds or elements which participate, as a reagent, in this reaction
- the catalytic system of the invention is usually in the form of a solution which is generally obtained by mixing and then reacting a first solution of the first reagent with a second solution of the second reagent then stirring These solutions are in solvents of the same type as those which were mentioned above.
- the mixture obtained from the two aforementioned solutions can be maintained and stirred, before its use, at a temperature which can be between -80 ° C and 110 ° C for a period of a few minutes a few hours, for example for an hour
- the system of the invention can be used for the polymerization or copolymerization of unsaturated compounds of the type of those described in the introduction to this description (olefins, dienes, (meth) acrylates) As compound of this type, mention may more particularly be made of ethylene, butadiene.
- the system of the invention is preferably used for the polymerization of ethylene. Mention may also be made of the polymerization of polar monomers of the (meth) acrylate type, iactone or lactide, preferably methyl methacrylate It will be noted that the system of the invention is suitable for block block copolymerization of ethylene with a polar monomer, in particular methyl methacrylate
- the polymerization is carried out under known conditions
- the polymerization temperature can be between -80 ° C. and 110 ° C. It is preferably worked at atmospheric pressure but it is also possible to work under pressure
- the reaction is usually carried out in the presence of a solvent which can be chosen in particular from aliphatic hydrocarbons or their mixtures such as butane, hexane, cyclohexane, aromatic hydrocarbons such as toluene
- Example 1 This example relates to the preparation of tert-butylates of different rare earths
- neodymium In a glove box, are weighed and placed in two Schlenk tubes of 100 ml, on the one hand sodium tertiobutylate (30mmol) and on the other hand anhydrous neodymium (III) (10mmol) These are then placed under argon and 40mL of THF are added to them respectively (distilled over K and degassed according to the freezing point technique) A solution of sodium tertiobutylate and a suspension are thus obtained of neodymium chloride The suspension of NdCI3 is transferred to a Schlenk tube with a minimum capacity of 300mL then the tBuONa solution is added to it.
- the two small Schlenk tubes are rinsed with 20mL of THF which will be added to the previous 80mL
- the mixture is maintained for 72 hours at room temperature with vigorous stirring and then the residual NaCl is left to settle overnight before filtering the solution which allows a clear blue solution to be obtained.
- the solvent for this solution is then evacuated under vacuum (10 2 mmHg) at room temperature for 5 to 6 hours.
- a light blue granular powder very soluble in toluene, is obtained with a yield of between 80 and 90%.
- the powdery product obtained can be re-installed in a solvent such as toluene or a toluene / pentane mixture (1/1) at -5 ° C.
- a solvent such as toluene or a toluene / pentane mixture (1/1) at -5 ° C.
- the X-ray diffraction analysis correlated by NMR analysis of the proton establishes that the compound has a formula like Nd 3 ( ⁇ 3-O t Bu) 2 ( ⁇ 2 -O t Bu) 3 ( ⁇ -O t Bu) 4 (THF) 2 THF
- the compound therefore does not contain chlorine
- the light blue powdery product and the crystallized product have the same catalytic properties
- Tm melting temperature of the polymer (determined by ATD)
- IP polymolecularity index (determined by GPC)
- the procedure is carried out using the same method as that described for Examples 2 to 10, but by injecting the mixture of rare earth tert-butoxide and the magnesium compound in 80 ml of toluene under 1 bar of ethylene placed at the desired reaction temperature. The consumption of ethylene is monitored by an instantaneous flowmeter and a totalizer. The polymer is precipitated in an acidified methanol solution (5% HCl). It is then filtered on a frit and dried in an oven at 60 ° C for 24 hours.
- polyethylenes prepared in the examples in the presence of Nd at low temperature (0 ° C) advantageously have a higher melting temperature than those of the polymers usually obtained.
- Physico-chemical analyzes show that the polymers obtained in these conditions are highly linear polymers with high molecular weights.
- the GPC analysis of the sample of example 11 reveals an Mn of 390000 and an IP of 2.1
- Neodymium tertiobutylate and d ⁇ (n-hexyl) magnesium are used in an Nd / Mg ratio of 1.
- the procedure is as described for Examples 2 to 10 with, however, the following modifications
- the mixing of the solutions which has been maintained for 1 hour at a temperature of 0 ° C. is injected into another Schlenk tube containing 80 ml of toluene saturated with ethylene (1 bar) at the polymerization temperature (0 ° C.)
- the polymerization of ethylene is carried out for 12 minutes
- the medium is purged with argon and the MAM is injected (50 mmol)
- the mixture is left stirring for one hour at 0 ° C.
- the reaction is stopped by adding a small amount of ethanol (1 to 2 ml ) and the polymer is precipitated in heptane
- the copolymer obtained is then filtered on filter and dried in an oven at 60 ° C for 24 hours 6.0g of the latter undergo extraction with acetone (at its point of boiling) for 48 hours in a Ku agawa apparatus.
- HomoPMMA is thus separated from homoPE and from the copolymer. Only 1.0 gram was dissolved in acetone, which amounts to saying that there is only 17%. homoPMMA in the polymer obtained
- the organomagnesium used is Mg (n-Hex) and the temperature at which the reaction between the alcoholate and the organo-magnesian is 0 ° C
- This example relates to the preparation of the tr ⁇ s (phenate) of neodymium Nd (O (2,6-'Bu-4- Me-C 6 H 2 ) 3 ) and its use in the polymerization of ethylene
- the neodymium t ⁇ s (phenate) is prepared as in Example 1 using sodium phenate in place of sodium tertiobutylate The other difference is that the reaction mixture is maintained for 72 hours at THF reflux. A fine powder is obtained purplish with a yield of 80-90%
- Example 2 For the polymerization, the procedure is as in Example 2 The mixing temperature of neodymium tr ⁇ s (phenate) and the magnesium compound is 20 ° C. The polymerization temperature is also 20 ° C. and the reaction time is d 'one o'clock
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Abstract
Description
SYSTEME CATALYTIQUE A BASE DE TERRE RARE ET DE MAGNESIUM, NOUVEL ALCOOLATE DE NEODYME, UTILISATION POUR LA POLYMERISATION DE CATALYTIC SYSTEM BASED ON RARE EARTH AND MAGNESIUM, NOVEL NEODYME ALCOOLATE, USE FOR THE POLYMERIZATION OF
COMPOSES INSATURESUNSATURATED COMPOUNDS
La présente invention concerne un système catalytique à base de terre rare et de magnésium, un nouvel alcoolate de néodyme et leur utilisation pour la polymérisation de composés insaturésThe present invention relates to a catalytic system based on rare earth and magnesium, a new neodymium alcoholate and their use for the polymerization of unsaturated compounds.
La polymérisation de composés à ιnsaturatιon(s) vιnylιque(s) (oléfines, dienes (méth)acrylates) comme l'éthylène ou le methacrylate de méthyle ou encore la copolymerisation de ce dernier avec les oléfines constituent actuellement un enjeu industriel important On a besoin de ce fait de catalyseurs ou d'amorceurs pour ces reactions de polymérisation qui soient toujours plus compétitifs en coût et en efficacité Notamment on cherche une efficacité améliorée en terme de tacticite et d'homodispersité On connaît ainsi des amorceurs du type métallocenes qui sont efficaces mais qui présentent l'inconvénient d'être difficiles à préparer et d'être coûteuxThe polymerization of compounds containing vinyl (olefins, dienes (meth) acrylates) such as ethylene or methyl methacrylate or the copolymerization of the latter with olefins is currently an important industrial issue. therefore catalysts or initiators for these polymerization reactions which are always more competitive in cost and efficiency. In particular, an improvement in tacticity and homodispersity efficiency is sought. Thus, initiators of the metallocene type are known which are effective but which have the disadvantage of being difficult to prepare and of being expensive
L'objet de l'invention est donc la mise au point d'un système catalytique performant et simple de préparationThe object of the invention is therefore the development of an efficient and simple preparation catalytic system
Dans ce but, le système catalytique selon l'invention est caractérisé en ce qu'il comprend un compose constitue par le produit de la réaction entreFor this purpose, the catalytic system according to the invention is characterized in that it comprises a compound constituted by the product of the reaction between
- un alcoolate de terre rare,- a rare earth alcoholate,
- un organo-magnésien- an organo-magnesian
Le système de l'invention est efficace et il permet, selon des modes de réalisation préférentiels, d'obtenir des polymères unimodaux, le cas échéant homodisperses et a taux de syndiotacticité élevéThe system of the invention is efficient and allows, according to preferred embodiments, to obtain unimodal polymers, if necessary homodispersed and with a high rate of syndiotacticity.
L'invention concerne aussi un alcoolate de néodyme qui est caractérisé en ce que l'alcoolate est un tertiobutylate ou un tertioamylate et en ce qu'il ne comporte pas de liaison covalente néodyme-chloreThe invention also relates to a neodymium alcoholate which is characterized in that the alcoholate is a tert-butylate or a tertioamylate and in that it does not contain a neodymium-chlorine covalent bond
D'autres caractéristiques, détails et avantages de l'invention apparaîtront encore plus complètement à la lecture de la description qui va suivre, ainsi que des divers exemples concrets mais non limitatifs destinés à l'illustrerOther characteristics, details and advantages of the invention will appear even more completely on reading the description which follows, as well as various concrete but nonlimiting examples intended to illustrate it.
Pour l'ensemble de la description, on entend par terre rare (TR) les éléments du groupe constitué par l'yttπum et les éléments de la classification périodique de numéro atomique compris inclusivement entre 57 et 71 Comme indiqué plus haut, le système catalytique de l'invention comprend un composé constitué par le produit de la réaction de deux réactifs qui vont être décrits plus précisément ci-dessous Le premier réactif est un alcoolate de terre rare. Par alcoolate, on entend les produits répondant à la formule (1) générale (TR)x(OR1)y(X)z(S)t dans laquelle R1 désigne un groupement organique, X un halogène et S un solvant coordinant et où x>1 , y>1 , z>0 et t>0. Le terme alcoolate s'applique aussi, dans le cadre de la présente invention, aux alcoolates de formule (1) comprenant plusieurs radicaux R1 différents. La terre rare de l'alcoolate peut être plus particulièrement l'yttrium, le lanthane, le cérium, le néodyme ou le samarium. Le néodyme est préféré.For the whole of the description, the term “rare earth” is understood to mean the elements of the group constituted by yttπum and the elements of the periodic classification with atomic number included inclusively between 57 and 71 As indicated above, the catalytic system of the invention comprises a compound consisting of the product of the reaction of two reagents which will be described more precisely below The first reagent is a rare earth alcoholate. By alcoholate is meant the products corresponding to the general formula (1) (TR) x (OR 1 ) y (X) z (S) t in which R 1 denotes an organic group, X a halogen and S a coordinating solvent and where x> 1, y> 1, z> 0 and t> 0. The term alcoholate also applies, in the context of the present invention, to alcoholates of formula (1) comprising several different radicals R 1 . The rare earth of the alcoholate can be more particularly yttrium, lanthanum, cerium, neodymium or samarium. Neodymium is preferred.
L'alcoolate est plus particulièrement un alcoolate d'un alcool ou d'un polyol dérivé d'un hydrocarbure aliphatique ou cyclique et notamment d'un hydrocarbure aliphatique, linéaire ou ramifié, en plus particulièrement en C4-C8. On peut mentionner tout particulièrement les alcoolates ou polyalcoolates tertiaires, par exemple le tertiobutylate ou le tertioamylate.The alcoholate is more particularly an alcoholate of an alcohol or of a polyol derived from an aliphatic or cyclic hydrocarbon and in particular from an aliphatic hydrocarbon, linear or branched, in more particularly in C 4 -C 8 . Mention may very particularly be made of tertiary alcoholates or polyalcoholates, for example tert-butylate or tertioamylate.
L'alcoolate peut aussi être un phénate, c'est à dire un dérivé d'un composé de type phénoiique ou polyphénolique. Selon un mode de réalisation préféré de l'invention, l'alcoolate est préparé par des procédés spécifiques qui vont être décrits plus précisément ci-dessous.The alcoholate can also be a phenate, that is to say a derivative of a compound of phenolic or polyphenolic type. According to a preferred embodiment of the invention, the alcoholate is prepared by specific methods which will be described more precisely below.
Un premier procédé met en œuvre une réaction d'un halogenure de terre rare avec un alcoolate d'alcalin ou d'alcalino-terreux. L'halogénure peut être plus particulièrement un chlorure et l'alcalin peut être notamment le sodium et le potassium. La réaction se fait en milieu solvant anhydre et à l'abri de l'air. Le milieu solvant est constitué par le tétrahydrofuranne (THF) ou comprend du tétrahydrofuranne en mélange avec un autre solvant. Comme autre solvant, on peut mentionner les hydrocarbures liquides de 3 à 12 atomes de carbone comme l'heptane, le cyclohexane, les hydrocarbures cycliques ou aromatiques comme le benzène, le toluène ou encore les xylènes. On peut mentionner aussi les éthers.A first method implements a reaction of a rare earth halide with an alkali or alkaline earth alcoholate. The halide can more particularly be a chloride and the alkali can be in particular sodium and potassium. The reaction is carried out in an anhydrous solvent medium and protected from air. The solvent medium is constituted by tetrahydrofuran (THF) or comprises tetrahydrofuran in mixture with another solvent. As other solvent, mention may be made of liquid hydrocarbons of 3 to 12 carbon atoms such as heptane, cyclohexane, cyclic or aromatic hydrocarbons such as benzene, toluene or even xylenes. We can also mention ethers.
La réaction a lieu généralement à une température qui peut être comprise entre l'ambiante (20°C) et 100°C sur une durée qui peut varier entre 12 heures environ et 96 heures environ. Dans le cas de la préparation d'un phénate, le mélange réactionnel est porté à reflux sur une durée du même ordre de grandeur. A l'issue de la réaction, on laisse décanter le milieu réactionnel, on évapore le surnageant et on obtient ainsi un produit solide, sous forme d'une poudre, qui constitue l'alcoolate de terre rare.The reaction generally takes place at a temperature which can be between ambient (20 ° C.) and 100 ° C. over a period which can vary between approximately 12 hours and approximately 96 hours. In the case of the preparation of a phenate, the reaction mixture is brought to reflux over a period of the same order of magnitude. At the end of the reaction, the reaction medium is allowed to settle, the supernatant is evaporated and a solid product is thus obtained, in the form of a powder, which constitutes the rare earth alcoholate.
Un second procédé spécifique consiste à faire réagir avec un alcoolate d'alcalin ou d'alcalino-terreux un adduit d'un halogenure de terre rare et de THF (TRX3,xTHF). Ce qui a été dit plus haut quant à la nature de l'alcoolate et de l'halogénure s'applique aussi ici. L'adduit peut être obtenu par chauffage d'un halogenure de terre rare dans le THF, par exemple à 50°C, puis évaporation du solvant. Cette évaporation peut se faire sous vide à 20°C. La réaction avec l'alcoolate a lieu aussi en milieu solvant anhydre et à l'abri de l'air et dans les mêmes conditions que celles décrites pour le procédé précédent Les solvants sont du même type que ceux donnés précédemment et on peut citer tout particulièrement le toluèneA second specific process consists in reacting with an alkali or alkaline earth alcoholate an adduct of a rare earth halide and THF (TRX 3 , xTHF). What has been said above as to the nature of the alcoholate and the halide also applies here. The adduct can be obtained by heating a rare earth halide in THF, for example at 50 ° C., then evaporation of the solvent. This evaporation can be done under vacuum at 20 ° C. The reaction with the alcoholate also takes place in an anhydrous solvent medium and away from air. and under the same conditions as those described for the previous process The solvents are of the same type as those given above and mention may be made very particularly of toluene
Un autre procédé spécifique peut être mentionné Ce procédé consiste à faire réagir un alcool avec un amidure de terre rare L'alcool peut être un alcool, un polyol ou un composé de type phénolique ou polyphénohque tels que définis plus haut L'amidure est un composé de formule TR(N(SιR2 3)2)3, R2 désignant un radical alkyl, par exemple méthyle La réaction se fait aussi en milieu solvant anhydre et à l'abri de l'air Le milieu solvant est constitué par le tétrahydrofuranne (THF) ou comprend du tétrahydrofuranne en mélange avec un autre solvant Comme autre solvant, on peut mentionner les hydrocarbures liquides de 3 à 12 atomes de carbone comme l'heptane, le cyclohexane, les hydrocarbures cycliques ou aromatiques comme le benzène, le toluène ou encore les xylènes On peut mentionner aussi les éthers La température de réaction peut être comprise entre -20°C et 100°C, mais généralement on travaille à température ambiante La durée de la réaction peut varier entre 15 minutes et 96 heures, elle peut être par exemple de 24 heuresAnother specific process can be mentioned. This process consists in reacting an alcohol with a rare earth amide. The alcohol can be an alcohol, a polyol or a phenolic or polyphenolic compound as defined above. The amide is a compound. of formula TR (N (SιR 2 3 ) 2 ) 3 , R 2 denoting an alkyl radical, for example methyl The reaction is also carried out in an anhydrous solvent medium and protected from air The solvent medium consists of tetrahydrofuran (THF) or comprises tetrahydrofuran in admixture with another solvent. As other solvent, mention may be made of liquid hydrocarbons of 3 to 12 carbon atoms such as heptane, cyclohexane, cyclic or aromatic hydrocarbons such as benzene, toluene or xylenes can also be mentioned ethers The reaction temperature can be between -20 ° C and 100 ° C, but generally one works at room temperature The reaction time can be short t vary between 15 minutes and 96 hours, it can be for example 24 hours
Enfin, un dernier procédé spécifique peut être décrit II consiste à faire reagir un alcool comme défini plus haut avec un adduit d'un amidure de terre rare tel que défini plus haut et de THF La préparation de l'adduit peut se faire de la même manière que celle donnée pour l'adduit décrit précédemment La suite du procédé est aussi du même type que ce qui a été décrit précédemment pour l'amidureFinally, a last specific process can be described. II consists in reacting an alcohol as defined above with an adduct of a rare earth amide as defined above and of THF. The preparation of the adduct can be done in the same way. manner as that given for the adduct described previously The rest of the process is also of the same type as that which was described previously for the amide
La présente invention concerne aussi, à titre de produit nouveau, un alcoolate de néodyme Cet alcoolate de néodyme présente comme caractéristique spécifique le fait qu'il ne comporte pas de chlore dans sa structure On notera que les alcoolates de terres rares connus, de par leur mode de préparation, présentent soit du chlore qui appartient à leur structure atomique même, soit un solvant ligandé, soit encore les deux à la fois En outre, pour ce produit, l'alcoolate est un tertiobutylate ou un tertioamylate L'alcoolate de néodyme de l'invention peut répondre à la formule Nd3(μ3-OtBu)2(μ2-OtBu)3(μ- OtBu)4(THF)2 nTHF ou Nd3(μ3-OtAm)2(μ2-OtAm)3(μ-OtAm)4(THF)2 nTHF, n pouvant être égal à 0 ou 1The present invention also relates, as a new product, to a neodymium alcoholate. This neodymium alcoholate has as specific characteristic the fact that it does not contain chlorine in its structure. It will be noted that the known rare earth alcoholates, by their mode of preparation, present either chlorine which belongs to their atomic structure even, or a liganded solvent, or both at the same time In addition, for this product, the alcoholate is a tert-butylate or a tertioamylate The neodymium alcoholate of the invention can correspond to the formula Nd 3 (μ3-O t Bu) 2 (μ 2 -O t Bu) 3 (μ- O t Bu) 4 (THF) 2 nTHF or Nd 3 (μ 3 -O t Am ) 2 (μ 2 -O t Am) 3 (μ-O t Am) 4 (THF) 2 nTHF, where n can be 0 or 1
L'absence de chlore peut être mis en évidence par analyse RX L'alcoolate de néodyme de l'invention peut être préparé en mettant en œuvre les procédés spécifiques qui ont été décrits ci-dessus en utilisant notamment le tertiobutylate ou un tertioamylate ou encore le tertiobutanol ou l'alcool tertiobutylique Le deuxième réactif entrant dans la réaction dont le produit constitue le composé du système catalytique de l'invention est un organo-magnésienThe absence of chlorine can be demonstrated by X-ray analysis. The neodymium alcoholate of the invention can be prepared by implementing the specific methods which have been described above, in particular using tert-butylate or a tertioamylate or else the tertiobutanol or tertiobutyl alcohol The second reagent used in the reaction, the product of which constitutes the compound of the catalytic system of the invention, is an organomagnesium
Par organo-magnésien, on entend un produit qui est soit un dialkyl-magnésien soit un réactif de Gπgnard Dans le cas d'un dialkyl-magnésien, c'est à dire les composés de formule (2) R- Mg-R' où R et R' désignent des radicaux alkyles, R et R' peuvent être notamment des radicaux en C C8, linéaires ou ramifiés, identiques ou différents R et R' peuvent être plus particulièrement le n-hexyle On peut aussi mentionner plus particulièrement le produit de formule (2) dans laquelle R et R' sont respectivement le butyle et l'ethyle Les radicaux alkyles R et/ou R' peuvent aussi porter un hétéroatome tel que Si On peut citer notamment le radical -CH2-Sι(CH3)3 By organo-magnesium is meant a product which is either a dialkyl-magnesian or a Gπgnard reagent In the case of a dialkyl-magnesian, that is to say the compounds of formula (2) R-Mg-R 'where R and R' denote alkyl radicals, R and R 'can be in particular radicals CC 8 , linear or branched, identical or different, R and R 'may more particularly be n-hexyl Mention may also be made more particularly of the product of formula (2) in which R and R' are respectively butyl and ethyl The alkyl radicals R and / or R 'can also carry a heteroatom such as Si Mention may in particular be made of the radical -CH 2 -Sι (CH 3 ) 3
L'organo-magnésien peut être aussi un réactif de Gπgnard, c'est à dire un composé de formule (3) R-Mg-X dans laquelle X désigne un halogène, l'halogène peut être le brome, le chlore ou l'iode mais on utilise plus particulièrement ceux pour lesquels l'halogène est le brome La nature de R peut être quelconque R peut être notamment un radical aliphatique saturé ou non ahcyclique ou aromatique R peut être plus particulièrement un radical alkyle, comme le radical éthyle, ou encore un radical phenyleThe organomagnesium can also be a Gπgnard reagent, that is to say a compound of formula (3) R-Mg-X in which X denotes a halogen, the halogen can be bromine, chlorine or iodine, but use is more particularly made of those for which the halogen is bromine The nature of R may be any R may in particular be a saturated or non-ahcyclic or aromatic aliphatic radical R may more particularly be an alkyl radical, such as the ethyl radical, another phenyl radical
L'alcoolate de terre rare et le composé du magnésium peuvent être mis en reaction dans des proportions respectives variables Cette proportion peut être exprimée par le rapport TR/Mg Ce rapport (rapport molaire) est compris généralement entre 0,5 et 5 II peut être plus particulièrement égal à 1 On ne sortirait pas toutefois du cadre de la présente invention en utilisant un rapport en dehors de la fourchette précitée Ce rapport peut varier notamment en fonction des composés insaturés que l'on cherche a polymenser On notera que l'utilisation d'un organo-magnésien de formule (2) ci-dessus dans laquelle R et R' sont respectivement le butyle et l'ethyle permet de travailler avec des rapports TR/Mg qui peuvent varier dans une fourchette assez largeThe rare earth alcoholate and the magnesium compound can be reacted in respective variable proportions This proportion can be expressed by the ratio TR / Mg This ratio (molar ratio) is generally between 0.5 and 5 It can be more particularly equal to 1 It would not, however, depart from the scope of the present invention to use a ratio outside the above-mentioned range. This ratio may vary in particular as a function of the unsaturated compounds which it is desired to polymerize. It will be noted that the use of 'an organo-magnesian of formula (2) above in which R and R' are respectively butyl and ethyl makes it possible to work with TR / Mg ratios which can vary within a fairly wide range
Le produit de la réaction des deux réactifs qui viennent d'être décrits constitue donc le compose du système catalytique de l'invention Par "constitue par le produit de la reaction des deux réactifs" on entend qu'il n'y a pas d'autres composés ou éléments qui participent, à titre de réactif, à cette réactionThe product of the reaction of the two reactants which have just been described therefore constitutes the compound of the catalytic system of the invention. By "consists of the product of the reaction of the two reactants" it is meant that there is no other compounds or elements which participate, as a reagent, in this reaction
Le système catalytique de l'invention se présente habituellement sous la forme d'une solution qui est obtenue généralement par mélange puis réaction d'une première solution du premier réactif avec une seconde solution du second réactif puis agitation Ces solutions sont dans des solvants du même type que ceux qui ont été mentionnes plus haut Le mélange obtenu à partir des deux solutions précitées peut être maintenu et agité, avant son utilisation, à une température qui peut être comprise entre -80°C et 110°C pendant une durée de quelques minutes à quelques heures, par exemple pendant une heure Le système de l'invention peut être utilisé pour la polymérisation ou la copolymerisation de composés insaturés du type de ceux décrits en introduction de la présente description (oléfines, diènes, (méth)acrylates) Comme composé de ce type, on peut mentionner plus particulièrement l'éthylène, le butadiène De préférence on utilise le système de l'invention pour la polymérisation de l'éthylène On peut citer aussi la polymérisation des monomères polaires du type (méth)acrylate, iactone ou lactide, de préférence le methacrylate de méthyle On notera que le système de l'invention convient à la copolymerisation séquencée bloc de l'éthylène avec un monomère polaire, notamment le methacrylate de méthyleThe catalytic system of the invention is usually in the form of a solution which is generally obtained by mixing and then reacting a first solution of the first reagent with a second solution of the second reagent then stirring These solutions are in solvents of the same type as those which were mentioned above The mixture obtained from the two aforementioned solutions can be maintained and stirred, before its use, at a temperature which can be between -80 ° C and 110 ° C for a period of a few minutes a few hours, for example for an hour The system of the invention can be used for the polymerization or copolymerization of unsaturated compounds of the type of those described in the introduction to this description (olefins, dienes, (meth) acrylates) As compound of this type, mention may more particularly be made of ethylene, butadiene. The system of the invention is preferably used for the polymerization of ethylene. Mention may also be made of the polymerization of polar monomers of the (meth) acrylate type, iactone or lactide, preferably methyl methacrylate It will be noted that the system of the invention is suitable for block block copolymerization of ethylene with a polar monomer, in particular methyl methacrylate
La polymérisation se fait dans les conditions connues La température de polymérisation peut se situer entre -80°C et 110°C On travaille de préférence à la pression atmosphérique mais il est aussi possible de travailler sous pression La reaction se fait habituellement en présence d'un solvant qui peut être choisi notamment parmi les hydrocarbures aliphatiques ou leurs mélanges comme le butane, l'hexane, le cyclohexane, les hydrocarbures aromatiques comme le toluèneThe polymerization is carried out under known conditions The polymerization temperature can be between -80 ° C. and 110 ° C. It is preferably worked at atmospheric pressure but it is also possible to work under pressure The reaction is usually carried out in the presence of a solvent which can be chosen in particular from aliphatic hydrocarbons or their mixtures such as butane, hexane, cyclohexane, aromatic hydrocarbons such as toluene
Dans le cas de la polymérisation de l'éthylène, il est possible de travailler en présence d'hydrogène comme agent de transfert ce qui permet, en particulier, de contrôler la longueur des chaînes des polymères formés Des exemples vont maintenant être donnésIn the case of the polymerization of ethylene, it is possible to work in the presence of hydrogen as a transfer agent, which makes it possible, in particular, to control the length of the chains of the polymers formed. Examples will now be given
Exemple 1 Cet exemple concerne la préparation de tertiobutylates de différentes terres raresExample 1 This example relates to the preparation of tert-butylates of different rare earths
On donne ci-dessous le mode opératoire dans le cas du néodyme Dans une boite à gants, sont pesés et placés dans deux tubes de Schlenk de 100mL, d'une part le tertiobutylate de sodium (30mmol) et d'autre part le chlorure de néodyme (III) anhydre (10mmol) Ceux-ci sont ensuite mis sous argon et on leur ajoute respectivement 40mL de THF (distillé sur K et dégazé suivant la technique du point de congélation) Sont ainsi obtenues une solution de tertiobutylate de sodium et une suspension de chlorure de néodyme La suspension de NdCI3 est transférée dans un tube de Schlenk d'une contenance minimale de 300mL puis on y ajoute la solution de tBuONa Les deux petits tubes de Schlenk sont rincés par 20mL de THF qui seront additionnés aux 80mL précédents Le mélange est maintenu pendant 72 heures à température ambiante sous forte agitation puis on laisse décanter le NaCI résiduel pendant une nuit avant de filtrer la solution ce qui permet d'obtenir une solution bleu limpide On évapore alors le solvant de cette solution sous vide (10 2mmHg) a température ambiante pendant 5 à 6 heures Une poudre bleu clair granuleuse très soluble dans le toluène, est obtenue avec un rendement compris entre 80 et 90%The procedure is given below in the case of neodymium. In a glove box, are weighed and placed in two Schlenk tubes of 100 ml, on the one hand sodium tertiobutylate (30mmol) and on the other hand anhydrous neodymium (III) (10mmol) These are then placed under argon and 40mL of THF are added to them respectively (distilled over K and degassed according to the freezing point technique) A solution of sodium tertiobutylate and a suspension are thus obtained of neodymium chloride The suspension of NdCI3 is transferred to a Schlenk tube with a minimum capacity of 300mL then the tBuONa solution is added to it. The two small Schlenk tubes are rinsed with 20mL of THF which will be added to the previous 80mL The mixture is maintained for 72 hours at room temperature with vigorous stirring and then the residual NaCl is left to settle overnight before filtering the solution which allows a clear blue solution to be obtained. the solvent for this solution is then evacuated under vacuum (10 2 mmHg) at room temperature for 5 to 6 hours. A light blue granular powder very soluble in toluene, is obtained with a yield of between 80 and 90%.
Le produit poudreux obtenu peut être recπstallisé dans un solvant tel que le toluène ou un mélange toluène/pentane (1/1) à -5°C L'analyse par diffraction des RX correlée par analyse RMN du proton établit que le composé a une formule du type Nd3(μ3-OtBu)2(μ2-OtBu)3(μ-OtBu)4(THF)2 THF Le composé ne comporte donc pas de chlore Ce composé cristallise dans le système orthorhombique dans le groupe Pbcn avec les paramètres de maille a=17,0538(10)A, b=20,0343(12) A, c=17,7400(11) AThe powdery product obtained can be re-installed in a solvent such as toluene or a toluene / pentane mixture (1/1) at -5 ° C. The X-ray diffraction analysis correlated by NMR analysis of the proton establishes that the compound has a formula like Nd 3 (μ3-O t Bu) 2 (μ 2 -O t Bu) 3 (μ-O t Bu) 4 (THF) 2 THF The compound therefore does not contain chlorine This compound crystallizes in the orthorhombic system in the group Pbcn with the mesh parameters a = 17.0538 (10) A, b = 20.0343 (12) A, c = 17.7400 (11) A
Le produit poudreux bleu clair et le produit cristallisé présentent les mêmes propriétés catalytiquesThe light blue powdery product and the crystallized product have the same catalytic properties
On procède de la même manière pour les tertiobutylates de céπum, d'yttnum, de lanthane et de samanumWe proceed in the same way for the tertiobutylates of cerum, yttnum, lanthanum and samanum
Les exemples qui suivent illustrent l'utilisation du système de l'invention dans la polymérisation de différents composés On donne ci-dessous la signification des différentes abréviations utilisées dans ces exemples n(TR) nombre de milhmoles de terre rare utiliséesThe examples which follow illustrate the use of the system of the invention in the polymerization of different compounds. The meanings of the different abbreviations used in these examples are given below n (TR) number of milhmoles of rare earth used
Tmel température à laquelle a été conduite la réaction entre l'alcoolate et l'organo-magnésienTmel temperature at which the reaction between the alcoholate and the organo-magnesium was carried out
T polym température à laquelle a été conduite la polymérisation t polym durée de la polymérisationT polym temperature at which the polymerization was carried out t polym duration of the polymerization
Tm température de fusion du polymère (déterminée par ATD)Tm melting temperature of the polymer (determined by ATD)
Rdt rendement de la polymérisationYield of polymerization
%rr pourcentage de syndiotacticité (déterminé par RMN du 1 H)% rr percentage of syndiotacticity (determined by 1 H NMR)
%mr pourcentage d'atacticité (déterminé par RMN du 1 H) %mm pourcentage d'isotacticité (déterminé par RMN du 1 H)% mr percentage of atacticity (determined by 1 H NMR)% mm percentage of isotacticity (determined by 1 H NMR)
IP indice de polymoléculaπté (déterminé par GPC)IP polymolecularity index (determined by GPC)
Mn masse molaire en nombre (déterminée par GPC)Mn molar mass in number (determined by GPC)
Cπst(%) pourcentage de cristallinité (déterminé par ATD)Cπst (%) percentage of crystallinity (determined by ATD)
Exemples 2 à 10Examples 2 to 10
Ces exemples illustrent l'utilisation du système de l'invention dans la polymérisation du methacrylate de méthyle (MAM)These examples illustrate the use of the system of the invention in the polymerization of methyl methacrylate (MAM)
Dans une boite à gants, on place dans un tube de Schlenk le tertiobutylate de terre rare obtenu dans l'exemple 1 (1 mmol) et dans un second tube le composé du magnésium en solution à 20% dans l'heptane Ceux-ci étant sous argon, on leur ajoute respectivement 10mL de toluène (distillé sur Na et dégazé) et on place les solutions ainsi obtenues à la température d'alkylation souhaitée On ajoute alors la solution de tertiobutylate de terre rare à celle du composé de magnésium Le mélange ainsi obtenu est maintenu pendant une heure à la température souhaitée puis injecté dans un autre tube de Schlenk où se trouvent 80mL de toluène à la température de polymérisation De suite, on injecte le MAM (50mmol) et on laisse sous agitation pendant une heure On arrête la réaction par ajout d'une petite quantité d'éthanol (1 à 2mL) et on précipite le polymère dans une solution d'éthanol acidifiée. Le polymère obtenu est filtré et lavé de nouveau à l'éthanol acidifié, filtré et séché pendant 24 heures à l'étuve à 60°C.In a glove box, place in a Schlenk tube the rare earth tert-butylate obtained in Example 1 (1 mmol) and in a second tube the magnesium compound in 20% solution in heptane These being under argon, 10 ml of toluene are added to them respectively (distilled over Na and degassed) and the solutions thus obtained are placed at the desired alkylation temperature. The solution of rare earth tert-butylate is then added to that of the magnesium compound. obtained is maintained for one hour at the desired temperature and then injected into another Schlenk tube in which 80 ml of toluene are found at the polymerization temperature. Immediately, the MAM (50 mmol) is injected and the mixture is left stirring for one hour. reaction by adding a small amount of ethanol (1 to 2 ml) and the polymer in an acidified ethanol solution. The polymer obtained is filtered and washed again with acidified ethanol, filtered and dried for 24 hours in an oven at 60 ° C.
On donne dans le tableau 1 ci-dessous la nature des composés du système catalytique utilisés et les conditions de polymérisation.The nature of the compounds of the catalytic system used and the polymerization conditions are given in table 1 below.
Tableau 1Table 1
On donne dans le tableau 2 ci-dessous les résultats de la polymérisation et les propriétés des polymères obtenus. Tableau 2The results of the polymerization and the properties of the polymers obtained are given in table 2 below. Table 2
'polymère non solubleinsoluble polymer
Exemples 11 à 18Examples 11 to 18
Ces exemples concernent l'utilisation du système de l'invention dans la polymérisation de l'éthylène.These examples relate to the use of the system of the invention in the polymerization of ethylene.
On procède en utilisant la même méthode que celle décrite pour les exemples 2 à 10 mais en injectant le mélange de tertiobutylate de terre rare et du composé de magnésium dans 80ml de toluène sous 1 bar d'éthylène placé à la température de réaction souhaitée. La consommation d'éthylène est suivie par un débitmètre instantané et un totaliseur. Le polymère est précipité dans une solution de méthanol acidifiée (5%HCI). Il est ensuite filtré sur fritte et séché à l'étuve à 60°C pendant 24 heures.The procedure is carried out using the same method as that described for Examples 2 to 10, but by injecting the mixture of rare earth tert-butoxide and the magnesium compound in 80 ml of toluene under 1 bar of ethylene placed at the desired reaction temperature. The consumption of ethylene is monitored by an instantaneous flowmeter and a totalizer. The polymer is precipitated in an acidified methanol solution (5% HCl). It is then filtered on a frit and dried in an oven at 60 ° C for 24 hours.
On donne dans le tableau 3 ci-dessous la nature des composés du système catalytique utilisé et les conditions de polymérisation. Dans tous les cas, la température d'alkylation est de 0°C.The nature of the compounds of the catalytic system used and the polymerization conditions are given in table 3 below. In all cases, the alkylation temperature is 0 ° C.
Tableau 3Table 3
On donne dans le tableau 4 ci-dessous les résultats de la polymérisation et les propriétés des polymères obtenus. Tableau 4The results of the polymerization and the properties of the polymers obtained are given in table 4 below. Table 4
* plusieurs pics * several peaks
Les polyéthylenes préparés dans les exemples en présence de Nd a basse température (0°C) présentent avantageusement une température de fusion plus élevée que celles des polymères obtenus habituellement Les analyses physico-chimiques (RMN, GPC et solubilité) montrent que les polymères obtenus dans ces conditions sont des polymères hautement linéaires et de masses moléculaires élevées Par exemple, l'analyse GPC de l'échantillon de l'exemple 11 révèle un Mn de 390000 et un IP de 2,1The polyethylenes prepared in the examples in the presence of Nd at low temperature (0 ° C) advantageously have a higher melting temperature than those of the polymers usually obtained. Physico-chemical analyzes (NMR, GPC and solubility) show that the polymers obtained in these conditions are highly linear polymers with high molecular weights. For example, the GPC analysis of the sample of example 11 reveals an Mn of 390000 and an IP of 2.1
Exemple 19Example 19
Cet exemple illustre la copolymerisation bibloc de l'éthylène et du methacrylate de méthyleThis example illustrates the biblock copolymerization of ethylene and methyl methacrylate
On utilise le tertiobutylate de néodyme et le dι(n-hexyl)magnésιum dans un rapport Nd/Mg de 1 On procède de la manière décrite pour les exemples 2 à 10 avec toutefois les modifications suivantes Le mélange des solutions qui a été maintenu 1 heure à la température de 0°C est injecté dans un autre tube de Schlenk où se trouvent 80mL de toluène saturé en éthylène (1 bar) à la température de polymérisation (0°C) La polymérisation de l'éthylène est menée pendant 12 minutes On arrête alors l'arrivée d'éthylène, on purge le milieu par de l'argon et on injecte le MAM (50mmol) On laisse sous agitation pendant une heure à 0°C La réaction est arrêtée par ajout d'une petite quantité d'éthanol (1 à 2mL) et on précipite le polymère dans l'heptane Le copolymère obtenu est ensuite filtré sur fπtté et séché à l'étuve à 60°C pendant 24 heures 6,0g de ce dernier subissent une extraction à l'acétone (à son point d'ébullition) pendant 48 heures dans un appareil de Ku agawa On sépare ainsi l'homoPMMA de l'homoPE et du copolymère Seulement 1 ,0 gramme était dissout dans l'acétone ce qui revient à dire qu'il n'y a que 17% d'homoPMMA dans le polymère obtenuNeodymium tertiobutylate and dι (n-hexyl) magnesium are used in an Nd / Mg ratio of 1. The procedure is as described for Examples 2 to 10 with, however, the following modifications The mixing of the solutions which has been maintained for 1 hour at a temperature of 0 ° C. is injected into another Schlenk tube containing 80 ml of toluene saturated with ethylene (1 bar) at the polymerization temperature (0 ° C.) The polymerization of ethylene is carried out for 12 minutes On then stop the arrival of ethylene, the medium is purged with argon and the MAM is injected (50 mmol) The mixture is left stirring for one hour at 0 ° C. The reaction is stopped by adding a small amount of ethanol (1 to 2 ml ) and the polymer is precipitated in heptane The copolymer obtained is then filtered on filter and dried in an oven at 60 ° C for 24 hours 6.0g of the latter undergo extraction with acetone (at its point of boiling) for 48 hours in a Ku agawa apparatus. HomoPMMA is thus separated from homoPE and from the copolymer. Only 1.0 gram was dissolved in acetone, which amounts to saying that there is only 17%. homoPMMA in the polymer obtained
On donne dans le tableau 5 ci-dessous les résultats obtenusThe results obtained are given in table 5 below.
Tableau 5Table 5
Exemples 20 à 22Examples 20 to 22
Ces exemples illustrent la polymérisation de l'éthylène en présence d'hydrogène comme agent de transfert On procède en utilisant la même méthode que celle décrite pour les exemples 11 à 18 mais en injectant un mélange d'éthylène/hydrogène (1 ,0 atm) à différente concentration en hydrogèneThese examples illustrate the polymerization of ethylene in the presence of hydrogen as a transfer agent. The procedure is carried out using the same method as that described for Examples 11 to 18 but by injecting a mixture of ethylene / hydrogen (1.0 atm). at different hydrogen concentration
On donne dans le tableau 6 ci-dessous la nature de la terre rare du système catalytique utilisé et les conditions de polymérisation Dans tous les cas l'organo- magnésien utilisé est Mg(n-Hex) et la température à laquelle a été conduite la réaction entre l'alcoolate et l'organo-magnésien est de 0°CThe nature of the rare earth of the catalytic system used and the polymerization conditions are given in table 6 below. In all cases, the organomagnesium used is Mg (n-Hex) and the temperature at which the reaction between the alcoholate and the organo-magnesian is 0 ° C
Tableau 6Table 6
On donne dans le tableau 7 ci-dessous des résultats de la polymérisation et les propriétés des polymères obtenus The results of the polymerization and the properties of the polymers obtained are given in table 7 below.
Tableau 7Table 7
'polymère non solubleinsoluble polymer
Exemple 23Example 23
Cet exemple concerne la préparation du trιs(phénate) de néodyme Nd(O(2,6-'Bu-4- Me-C6H2)3) et son utilisation dans la polymérisation de l'éthylèneThis example relates to the preparation of the trιs (phenate) of neodymium Nd (O (2,6-'Bu-4- Me-C 6 H 2 ) 3 ) and its use in the polymerization of ethylene
Le tπs(phénate) de néodyme est préparé comme dans l'exemple 1 en utilisant du phénate de sodium en place du tertiobutylate de sodium L'autre différence est que le mélange réactionnel est maintenu pendant 72 heures à reflux du THF On obtient une poudre fine violacée avec un rendement de 80-90%The neodymium tπs (phenate) is prepared as in Example 1 using sodium phenate in place of sodium tertiobutylate The other difference is that the reaction mixture is maintained for 72 hours at THF reflux. A fine powder is obtained purplish with a yield of 80-90%
Pour la polymérisation, on procède comme dans l'exemple 2 La température de mélange du trιs(phénate) de néodyme et du composé de magnésium est de 20 °C La température de polymérisation est aussi de 20 °C et le temps de réaction est d'une heureFor the polymerization, the procedure is as in Example 2 The mixing temperature of neodymium trιs (phenate) and the magnesium compound is 20 ° C. The polymerization temperature is also 20 ° C. and the reaction time is d 'one o'clock
Lors de cette réaction, 750 mg d'éthylène sont consommés et après précipitation et filtration 450 mg de polyéthylène sont obtenus During this reaction, 750 mg of ethylene are consumed and after precipitation and filtration 450 mg of polyethylene are obtained
Claims
Priority Applications (7)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2001508233A JP2003504429A (en) | 1999-07-05 | 2000-06-30 | Rare earth and magnesium based catalyst systems, new neodymium alcoholates and their use in the polymerization of unsaturated compounds |
| MXPA02000038A MXPA02000038A (en) | 1999-07-05 | 2000-06-30 | Catalytic system based on rare earth and magnesium. novel neodymium alcoholate, use for polymerising unsaturated compounds. |
| CA002378450A CA2378450A1 (en) | 1999-07-05 | 2000-06-30 | Catalytic system based on rare earth and magnesium. novel neodymium alcoholate, use for polymerising unsaturated compounds |
| EP00949599A EP1200490A1 (en) | 1999-07-05 | 2000-06-30 | Catalytic system based on rare earth and magnesium. novel neodymium alcoholate, use for polymerising unsaturated compounds |
| KR1020027000118A KR20020037328A (en) | 1999-07-05 | 2000-06-30 | Catalytic System Based on Rare Earth and Magnesium, Novel Neodymium Alcoholate, Use for Polymerising Unsaturated Compounds |
| BR0012165-7A BR0012165A (en) | 1999-07-05 | 2000-06-30 | Catalytic system, neodymium alcoholate, and, polymerization or copolymerization process of, an unsaturated compound |
| NO20020040A NO20020040L (en) | 1999-07-05 | 2002-01-04 | Catalytic system based on rare earth metal, a new neodymium alcoholate and application for polymerization of unsaturated compounds |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR99/08648 | 1999-07-05 | ||
| FR9908648A FR2795976B1 (en) | 1999-07-05 | 1999-07-05 | CATALYTIC SYSTEM BASED ON RARE EARTH AND MAGNESIUM, NOVEL NEODYME ALCOOLATE, USE FOR THE POLYMERIZATION OF UNSATURATED COMPOUNDS |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2001002446A1 true WO2001002446A1 (en) | 2001-01-11 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/FR2000/001863 Ceased WO2001002446A1 (en) | 1999-07-05 | 2000-06-30 | Catalytic system based on rare earth and magnesium. novel neodymium alcoholate, use for polymerising unsaturated compounds |
Country Status (11)
| Country | Link |
|---|---|
| EP (1) | EP1200490A1 (en) |
| JP (1) | JP2003504429A (en) |
| KR (1) | KR20020037328A (en) |
| BR (1) | BR0012165A (en) |
| CA (1) | CA2378450A1 (en) |
| FR (1) | FR2795976B1 (en) |
| MX (1) | MXPA02000038A (en) |
| NO (1) | NO20020040L (en) |
| TW (1) | TW567190B (en) |
| WO (1) | WO2001002446A1 (en) |
| ZA (1) | ZA200200012B (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2819199A1 (en) * | 2001-01-09 | 2002-07-12 | Rhodia Elect & Catalysis | CATATYTIC SPECIES BASED ON RARE EARTH AND MAGNESIUM, ITS USE IN THE POLYMERIZATION OF AN OLEFIN OR LACTONE AND OBTAINED (METH) ACRYLIC DIBLOCS ETHYLENE-CO-ESTERS COPOLYMERS |
| WO2002094898A3 (en) * | 2001-05-18 | 2003-11-20 | Rhodia Elect & Catalysis | Block copolymer preparation method |
| US8889653B2 (en) | 2002-06-25 | 2014-11-18 | Rhodia, Inc. | Grafting polymerization of guar and other polysaccharides by electron beams |
| CN105218451A (en) * | 2015-10-20 | 2016-01-06 | 复旦大学 | A kind of method of narrowing of rare earth catalyst ring Reactive Synthesis imidazolidine derivatives |
| CN105237481A (en) * | 2015-10-20 | 2016-01-13 | 复旦大学 | Method for synthesizing 1, 4, 5, 6-tetrahydropyrimidine derivative through rare earth catalysis |
| WO2022229536A1 (en) * | 2021-04-29 | 2022-11-03 | Compagnie Generale Des Etablissements Michelin | Functional copolymer of a 1,3-diene and ethylene or a 1,3-diene, ethylene and an alpha-monoolefin |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2946048B1 (en) * | 2009-06-02 | 2012-12-28 | Michelin Soc Tech | CATALYTIC SYSTEM FOR POLYMERIZATION OF CONJUGATED DIENES, POLYMERISATION METHOD AND FUNCTIONAL POLYMER OBTAINED |
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| US4520177A (en) * | 1983-05-24 | 1985-05-28 | Jenkins Derek K | Polymerization of conjugated dienes |
| EP0304088A1 (en) * | 1987-08-19 | 1989-02-22 | Asahi Kasei Kogyo Kabushiki Kaisha | A prepolymerization process for producing a conjugated diene compound prepolymer solution |
| EP0667357A1 (en) * | 1994-02-11 | 1995-08-16 | ENICHEM ELASTOMERI S.r.l. | Catalytic system and process for the production of polydiolefins |
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- 1999-07-05 FR FR9908648A patent/FR2795976B1/en not_active Expired - Fee Related
-
2000
- 2000-06-30 WO PCT/FR2000/001863 patent/WO2001002446A1/en not_active Ceased
- 2000-06-30 KR KR1020027000118A patent/KR20020037328A/en not_active Ceased
- 2000-06-30 JP JP2001508233A patent/JP2003504429A/en active Pending
- 2000-06-30 MX MXPA02000038A patent/MXPA02000038A/en unknown
- 2000-06-30 EP EP00949599A patent/EP1200490A1/en not_active Withdrawn
- 2000-06-30 BR BR0012165-7A patent/BR0012165A/en not_active Application Discontinuation
- 2000-06-30 CA CA002378450A patent/CA2378450A1/en not_active Abandoned
- 2000-07-04 TW TW089113221A patent/TW567190B/en active
-
2002
- 2002-01-02 ZA ZA200200012A patent/ZA200200012B/en unknown
- 2002-01-04 NO NO20020040A patent/NO20020040L/en not_active Application Discontinuation
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| US4520177A (en) * | 1983-05-24 | 1985-05-28 | Jenkins Derek K | Polymerization of conjugated dienes |
| EP0304088A1 (en) * | 1987-08-19 | 1989-02-22 | Asahi Kasei Kogyo Kabushiki Kaisha | A prepolymerization process for producing a conjugated diene compound prepolymer solution |
| EP0667357A1 (en) * | 1994-02-11 | 1995-08-16 | ENICHEM ELASTOMERI S.r.l. | Catalytic system and process for the production of polydiolefins |
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2819199A1 (en) * | 2001-01-09 | 2002-07-12 | Rhodia Elect & Catalysis | CATATYTIC SPECIES BASED ON RARE EARTH AND MAGNESIUM, ITS USE IN THE POLYMERIZATION OF AN OLEFIN OR LACTONE AND OBTAINED (METH) ACRYLIC DIBLOCS ETHYLENE-CO-ESTERS COPOLYMERS |
| WO2002055193A3 (en) * | 2001-01-09 | 2003-01-03 | Rhodia Elect & Catalysis | Type of catalyst made from a rare earth and magnesium, use thereof in olefin or lactone polymerisation and the ethylene (meth)acrylic co-ester diblock copolymers obtained |
| WO2002094898A3 (en) * | 2001-05-18 | 2003-11-20 | Rhodia Elect & Catalysis | Block copolymer preparation method |
| US8889653B2 (en) | 2002-06-25 | 2014-11-18 | Rhodia, Inc. | Grafting polymerization of guar and other polysaccharides by electron beams |
| CN105218451A (en) * | 2015-10-20 | 2016-01-06 | 复旦大学 | A kind of method of narrowing of rare earth catalyst ring Reactive Synthesis imidazolidine derivatives |
| CN105237481A (en) * | 2015-10-20 | 2016-01-13 | 复旦大学 | Method for synthesizing 1, 4, 5, 6-tetrahydropyrimidine derivative through rare earth catalysis |
| CN105237481B (en) * | 2015-10-20 | 2018-07-13 | 复旦大学 | A kind of method of rare earth catalyst synthesis 1,4,5,6- tetrahydropyrimidinederivatives derivatives |
| WO2022229536A1 (en) * | 2021-04-29 | 2022-11-03 | Compagnie Generale Des Etablissements Michelin | Functional copolymer of a 1,3-diene and ethylene or a 1,3-diene, ethylene and an alpha-monoolefin |
| FR3122428A1 (en) * | 2021-04-29 | 2022-11-04 | Compagnie Generale Des Etablissements Michelin | functional copolymer of a 1,3-diene and ethylene or of a 1,3-diene, ethylene and an alpha-monoolefin. |
| CN117222677A (en) * | 2021-04-29 | 2023-12-12 | 米其林集团总公司 | Functional copolymers of 1, 3-dienes with ethylene or functional copolymers of 1, 3-dienes, ethylene with alpha-mono-olefins |
Also Published As
| Publication number | Publication date |
|---|---|
| ZA200200012B (en) | 2003-02-03 |
| FR2795976B1 (en) | 2001-10-05 |
| EP1200490A1 (en) | 2002-05-02 |
| KR20020037328A (en) | 2002-05-18 |
| TW567190B (en) | 2003-12-21 |
| FR2795976A1 (en) | 2001-01-12 |
| JP2003504429A (en) | 2003-02-04 |
| CA2378450A1 (en) | 2001-01-11 |
| NO20020040D0 (en) | 2002-01-04 |
| BR0012165A (en) | 2002-06-18 |
| NO20020040L (en) | 2002-03-05 |
| MXPA02000038A (en) | 2004-08-12 |
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