US20020010084A1 - Method for producting fulvene metal complexes - Google Patents
Method for producting fulvene metal complexes Download PDFInfo
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- US20020010084A1 US20020010084A1 US09/922,365 US92236501A US2002010084A1 US 20020010084 A1 US20020010084 A1 US 20020010084A1 US 92236501 A US92236501 A US 92236501A US 2002010084 A1 US2002010084 A1 US 2002010084A1
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- MCEJJXNBAPNTMY-UHFFFAOYSA-N CC(C)=C1C(C)=C(C)C(C)=C1C Chemical compound CC(C)=C1C(C)=C(C)C(C)=C1C MCEJJXNBAPNTMY-UHFFFAOYSA-N 0.000 description 7
- WWWGOVOVYRKPEQ-UHFFFAOYSA-M CC(C)=C1C(C)=C(C)C2=C1C=CC=C2.[V]I Chemical compound CC(C)=C1C(C)=C(C)C2=C1C=CC=C2.[V]I WWWGOVOVYRKPEQ-UHFFFAOYSA-M 0.000 description 1
- RJLCZHXAOWIDAO-UHFFFAOYSA-N CC(C)=C1C2=C(C=CC=C2)C2=C1C=CC=C2.[V] Chemical compound CC(C)=C1C2=C(C=CC=C2)C2=C1C=CC=C2.[V] RJLCZHXAOWIDAO-UHFFFAOYSA-N 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F17/00—Metallocenes
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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
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/02—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
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/04—Monomers containing three or four carbon atoms
- C08F110/06—Propene
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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
- C08F4/60—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 together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
- C08F4/65908—Component covered by group C08F4/64 containing a transition metal-carbon bond in combination with an ionising compound other than alumoxane, e.g. (C6F5)4B-X+
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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
- C08F4/60—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 together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
- C08F4/65912—Component covered by group C08F4/64 containing a transition metal-carbon bond in combination with an organoaluminium compound
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10S526/00—Synthetic resins or natural rubbers -- part of the class 520 series
- Y10S526/941—Synthetic resins or natural rubbers -- part of the class 520 series having the transition metal bonded directly to carbon
Definitions
- the present invention relates to a process for the preparation of fulvene-metal complexes, new fulvene-metal complexes and their use as catalysts for the polymerization of unsaturated compounds, in particular for the polymerization and copolymerization of olefins and/or dienes.
- Metal complexes with cyclopentadienyl ligands have been the subject of intense investigation since the discovery of ferrocene.
- the use of cyclopentadienyl-metal complexes, in particular the use of metallocene complexes as a mixture with activating cocatalysts, preferably alumoxanes, for the polymerization of olefins and diolefins has been known for a long time (e.g. EP-A 69 951, 129 368, 351 392, 485 821, 485 823).
- Metallocenes have proved to be highly active, specific catalysts in the polymerization of olefins.
- thermolysis reaction The synthesis of the ( ⁇ 6 -2,3,4,5-tetramethylcyclopentadienyl-1-methylene)( ⁇ 5 -pentamethylcyclopentadienyl)zirconium compound is very expensive, it first being necessary to prepare a metallocene with pentamethylcyclopentadienyl ligands, which is decomposed by a thermolysis reaction in the last synthesis stage. Such thermolysis reactions are described in the literature.
- the fulvene complex ( ⁇ 6 -2,3,4,5-tetramethylcyclopentadienyl-1-methylene)( ⁇ 5 -pentamethylcyclopentadienyl)titanium-methyl is formed by thermolysis of bis( ⁇ 5 -pentamethylcyclopentadienyl)titanium-dimethyl.
- T. J. Marks et al., JACS (1988), 110, 7701 describe the thermolysis of pentamethylcyclopentadienyl complexes of zirconium and hafnium.
- the fulvene complex ( ⁇ 6 -2,3,4,5-tetramethylcyclopentadienyl-1-methylene) ⁇ 5 -pentamethylcyclopentadienyl)zirconium-phenyl is formed by thermnolysis of bis( ⁇ 5 -pentamethylcyclopentadienyl)zirconium-diphenyl.
- fulvene-metal complexes can be prepared by reaction of a fulvene compound with a suitable transition metal complex in the presence of a reducing agent.
- the present invention thus provides a process for the preparation of fulvene-metal complexes of the formula (Ia)
- M is a metal from group IIIb, IVb, Vb or VIb or the lanthanides or the actinides of the periodic table of the elements according to IUPAC,
- A denotes an anionic ligand optionally with one or more bridges
- X denotes a hydrogen atom, a C 1 - to C 10 -alkyl group, a C 1 - to C 10 -alkoxy group, a C 6 - to C 10 -aryl group, a C 6 - to C 10 -aryloxy group, a C 2 - to C 10 -alkenyl group, a C 7 - to C 40 -arylalkyl group, a C 7 -to C 40 -alkylaryl group, a C 8 - to C 40 -arylalkenyl group, a silyl group substituted by C 1 - to C 10 -hydrocarbon radicals, a halogen atom or an amide of the formula NR 7 2 ,
- L denotes a neutral ligand
- R 1 , R 2 , R 3 , R 4 , R 5 , R 6 are identical or different and represent hydrogen, halogen, a cyano group, a C 1 - to C 20 -alkyl group, a C 1 - to C 10 -fluoroalkyl group, a C 6 - to C 10 -fluoroaryl group, a C 1 - to C 10 -alkoxy group, a C 6 - to C 20 -aryl group, a C 6 - to C 10 -aryloxy group, a C 2 - to C 10 -alkenyl group, a C 7 - to C 40 -arylalkyl group, a C 7 - to C 40 -alkylaryl group, a C 1 - to C 40 -arylalkenyl group, a C 2 - to C 10 - alkinyl group, a silyl group substituted by C 1 -C 10 -hydrocarbon radicals
- R 1 , R 2 , R 3 , R 4 , R 5 , R 6 in each case together with the atoms connecting them, form one or more aliphatic or aromatic ring systems, which can contain one or more heteroatoms (O, N, S) and 5 to 10 carbon atoms,
- R 7 represents hydrogen, a C 1 - to C 20 -alkyl group, a C 6 - to C 20 -aryl group, a C 7 - to C 40 -arylalkyl group, a C 7 - to C 40 -alkylaryl group, a silyl group substituted by C 1 -C 10 -hydrocarbon radicals or an amino group which is optionally substituted by C 1 -C 20 -hydrocarbon radicals,
- m, p represent the numbers 0, 1, 2, 3 or 4, which result from the valency and the bonding state of M, and
- k represents the number 1, 2 or 3, and the sum of k+m+p is 1 to 5, depending on the oxidation level of M, and
- n is a number from 0 to 10
- s is 2, 3, 4, 5 or 6 and s is >p
- R 1 , R 2 , R 3 , R 4 , R 5 and R 6 have the abovementioned meaning
- the reaction can be carried out in a single reaction step, i.e. in a one-pot reaction, the sequence of addition of the individual reaction components not being fixed.
- the reaction can also be carried out in separate reaction steps.
- transition metal compounds of the formula (IIa) or (IIb) can first be brought into contact with a reducing agent and reacted with fulvene compounds of the formula (III) in a separate reaction step. It is furthermore preferable first to add the transition metal compound (IIa) or (IIb) to the fulvene compound (III) and then to add the reducing agent.
- suitable reducing agents are alkali metals, alkaline earth metals, aluminium, zinc, alloys of the alkali metals, such as e.g. sodium-potassium alloys or sodium amalgam, alloys of the alkaline earth metals, and metal hydrides.
- metal hydrides are lithium hydride, sodium hydride, magnesium hydride, aluminium hydride, lithium aluminium hydride and sodium borohydride.
- Specific examples of reducing agents are sodium naphthalenide, potassium graphite, lithium-alkyls, magnesium-butadiene, magnesium-anthracene, trialkylaluminium compounds and Grignard reagents.
- Preferred reducing agents are alkali metals or alkaline earth metals, C 1 -C 6 -alkyllithium, tri-C 1 -C 6 -alkylaluminium compounds and Grignard reagents.
- Preferred reducing agents are lithium, magnesium, n-butyllithium and triethylaluminium and triisobutylaluminium. Instead of the reducing agents mentioned, it is also possible to carry out an electrochemical reduction.
- the process for the preparation of the fulvene-metal complexes of the formula (I) is carried out in a suitable reaction medium at temperatures of ⁇ 100 to +250° C., preferably ⁇ 78 to +130° C., particularly preferably ⁇ 10 to +120° C.
- reaction media examples include aliphatic or aromatic hydrocarbons, halogenated hydrocarbons, ethers and cyclic ethers.
- examples of these are unbranched aliphatic hydrocarbons, such as butane, pentane, hexane, heptane and octane, branched aliphatic hydrocarbons, such as isobutane, isopentane and isohexane, cyclic aliphatic hydrocarbons, such as cyclohexane and methylcyclohexane, aromatic hydrocarbons, such as benzene, toluene and xylene, and ethers, such as dialkyl ethers, dimethoxyethane and tetrahydrofuran. Mixtures of various solvents are also suitable.
- the fulvene-metal complexes of the formula (I) are prepared and handled with the exclusion of air and water under inert gas conditions (inert gas technique).
- inert gases are nitrogen or argon.
- the Schlenk technique generally conventional for organometallic substances is suitable, for example, as an inert gas technique.
- the fulvene-metal complexes of the formula (I) can be isolated or employed directly for further reactions. If isolation is necessary, the by-products formed can be removed by conventional methods of purification, e.g. by filtration. Alternatively, the desired products can also be extracted with a solvent. If necessary, a purification operation, e.g. recrystallization, can be carried out.
- Possible transition metal complexes of the formula (IIa) or (IIb) are, in particular, those in which
- M is a metal from the group consisting of titanium, zirconium, hafnium, vanadium, niobium, tantalum and chromium,
- A is a pyrazolate of the formula N 2 C 3 R 8 3 where R 8 represents hydrogen or a C 1 -C 10 -alkyl group or a C 6 -C 10 -aryl group, a pyrazolylborate of the formula R 7 B(N 2 C 3 R 8 3 ) 3 , an alcoholate or phenolate of the formula OR 7 , a siloxane of the formula OSiR 7 3 , a thiolate of the formula SR 7 , an acetylacetonate of the formula (R 7 CO) 2 CR 7 , a diimine of the formula (R 7 N ⁇ CR 7 ) 2 , an amidinate of the formula R 7 C(NR 7 2 ) 2 , a cyclooctatetraenyl of the formula C 8 H q R 7 8-q where q is 0, 1, 2, 3, 4, 5, 6 or 7 , a cyclopentadienyl of the formula C 5 H q R 7 5-q where
- L, X, R 7 , m, s and n have the abovementioned meaning.
- transition metal complexes of the formula (IIa) or (IIb) are those in which
- M represents titanium, zirconium or hafnium
- A represents bis(trimethylsilyl)amide, dimethylamide, diethylamide, diisopropylamide, 2,6-di-tert-butyl-4-methylphenolate, cyclooctatetraenyl, cyclopentadienyl, methylcyclopentadienyl, benzylcyclopentadienyl, n-propylcyclopentadienyl, n-butylcyclopentadienyl, iso-butylcyclopentadienyl, t-butylcyclopentadienyl, cyclopentylcyclopentadienyl, octadecylcyclopentadienyl, 1,2-dimethylcyclopentadienyl, 1,3-dimethylcyclopentadienyl, 1,3-diisopropylcyclopentadienyl, 1,3-di-t-butylcyclopentadien
- X denotes fluorine or chlorine
- L, m, s and n have the abovementioned meaning.
- Possible fulvene compounds are, in particular, those of the formula (III) in which
- R 1 to R 6 represents a C 1 -C 30 -alkyl group, a C 6 -C 10 -aryl group or a C 7 -C 40 -alkylaryl group, in particular hydrogen, methyl, trifluoromethyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, tert-butyl, phenyl, pentafluorophenyl, methylphenyl, cyclohexyl or benzyl.
- Preferred compounds of the formula (III) are fulvene compounds of the fonnula (IV)
- R 1 , R 2 , R 3 and R 4 have the abovementioned meaning.
- Particularly preferred compounds of the formula (III) are 6-cyclohexylfulvene, 6-isopropylfulvene, 6-tert-butylfulvene, 6-phenylfulvene, 6-(dimethylamino)fulvene, 6,6-bis(dimethylamino)fulvene, 6,6-dimethylfulvene, 6,6-bis(trifluoromothyl)-fulvene, 6,6-diphenylfulvene, 6,6-bis(pentafluorophenyl)fulvene, 6,6-pentamethylenefulvene, 6,6-tetramethylenefulvene, 6,6-trimethylenefulvene, 2-(2,4-cyclopentadien-1-ylidene)-1,3-dithiolane, 5-benzylidene-1,2,3-triphenyl-1,3-cyclopentadiene, 1,2,3,4-tetramethylfulvene, 1,2,3,4-tetraphenylful
- FIG. 1 shows in perspective the structure of a fulvene-metal complex which can be prepared according to the invention such as is obtained by X-ray structure analysis, taking the compound (6-tert-butylfulvenyl)pentamethylcyclopentadienyl)titanium chloride as an example.
- the process according to the invention opens up an access to new fulvene-metal complexes of the formula (I) which e.g. cannot be formed by thermolysis.
- the present invention therefore also provides fulvene-metal complexes of the formula (I) in which
- M is a metal from the group consisting of titanium, zirconium, hafnium, vanadium, niobium, tantalum and chromium,
- R 1 and R 2 represent hydrogen and at the same time
- R 3 , R 4 , R 5 and R 6 represent a methyl group and at the same time
- A denotes a pentamethylcyclopentadienyl group or a carboranediyl group of the formula C 2 B 9 11 11 .
- the present invention also provides a catalyst system comprising a
- M is a metal from the group consisting of titanium, zirconium, hafnium, vanadium, niobium, tantalum and chromium,
- Possible cocatalysts are the cocatalysts known in the field of metallocene catalysis, such as polymeric or oligomeric aluminoxanes, Lewis acids and aluminates and borates.
- metallocene catalysis such as polymeric or oligomeric aluminoxanes, Lewis acids and aluminates and borates.
- Particularly suitable cocatalysts are methylaluminoxane, methylalumoxane and diisobutylalumoxane modified by triisobutylaluminium, trialkylaluminium compounds, such as trimethylaluminium, triethylaluminium, triisobutylaluminium and trilsooctylaluminium, and furthermore dialkylaluminium compounds, such as diisobutylaluminium hydride, diisobutylaluminium fluoride and diethylaluminium chloride, substituted triarylaluminium compounds, such as tristpentafluorophenyl)aluminium, and ionic compounds which contain tetrakis(pentafluorophenyl)aluminate as the anion, such as triphenylmethyl tetrakis(pentafluorophenyl)aluminate and N,N-dimethylanilini
- the present invention also provides the use of the new catalyst system for the polymerization of unsaturated compounds, in particular olefins and dienes. Both homopolymerization and copolymerization of the unsaturated compounds mentioned are understood as polymerization here.
- Compounds which are employed in particular in the polymerization are C 2 -C 10 -alkenes, such as ethylene, propylene, but-1-ene, pent-1-ene and hex-1-ene, oct-1-ene and isobutylene, and arylalkenes, such as styrene.
- Dienes which are employed in particular are: conjugated dienes, such as 1,3-butadiene, isoprene and 1,3-pentadiene, and non-conjugated dienes, such as 1,4-hexadiene, 1,5-heptadiene, 5,7-dimethyl-1,6-octadiene, 4-vinyl-1-cyclohexene, 5-ethylidene-2-norbornene, 5-vinyl-2-norbornene and dicyclopentadiene.
- conjugated dienes such as 1,3-butadiene, isoprene and 1,3-pentadiene
- non-conjugated dienes such as 1,4-hexadiene, 1,5-heptadiene, 5,7-dimethyl-1,6-octadiene, 4-vinyl-1-cyclohexene, 5-ethylidene-2-norbornene, 5-vinyl-2-norbornene and dicyclopenta
- the catalysts according to the invention are suitable for the preparation of rubbers based on copolymers of ethylene with one or more of the ⁇ -olefins mentioned and the dienes mentioned.
- the catalyst system according to the invention is furthermore suitable for the polymerization of cyclo-olefins, such as norbornene, cyclopentene, cyclohexene and cyclooctene, and the copolymerization of cycloolefins with ethylene or ⁇ -olefins.
- the polymerization can be carried out in the liquid phase, in the presence or absence of an inert solvent or in the gas phase.
- Suitable solvents are aromatic hydrocarbons, such as benzene and/or toluene, or aliphatic hydrocarbons, such as propane, hexane, heptane, octane, isobutane or cyclohexane, or mixtures of the various hydrocarbons.
- Suitable support materials which may be mentioned are e.g.: inorganic or organic polymeric supports, such as silica gel, zeolites, carbon black, active charcoal, aluminium oxide, polystyrene and polypropylene.
- the catalyst system according to the invention can be applied here to the support materials in the conventional manner.
- Methods of supporting catalyst systems are described, for example, in U.S. Pat. Nos. 4,808,561, 4,912,075, 5,008,228 and 4,914,253.
- the polymerization is in general carried out under pressures of 1 to 1,000, preferably 1 to 100 bar and at temperatures of ⁇ 100 to +250° C., preferably 0 to +150° C.
- the polymerization can be carried out continuously or discontinuously in conventional reactors.
- Fulvene complex synthesis by reaction of 6,6-dimethylfulvene with Cp*TiCl 3 , in the presence of butyllithium [(Cp*)(C 5 H 4 C(CH 3 ) 2 )TiCl]400 mg (1.38 mmol) Cp*TiCl 3 , 154 mg (1.45 mmol) 6,6-dimethylfulvene and 1.11 ml (2.76 mmol) n-butyllithium were combined in 25 ml THF in a Schlenk vessel at a temperature of ⁇ 78° C. The mixture was allowed to warm slowly to 0° C. and was stirred for a further two hours at this temperature in order to bring the reaction to completion.
Abstract
The invention relates to a process for the preparation of polyolefins by polymerizing olefins of the formula CH2CHR in which R=H or C1-C10 alkyl, on their own or as a mixture, if appropriate together with C4-C12 α,ω-diolefins, in solvents, liquid monomers or the gas phase, at temperatures between −50° and 200° C., using a catalyst system composed of a soluble, halogen-containing transition metal compound of the general formula
(cyclopentadienyl)2 Me R Hal
in which R is cyclopentadienyl or a C1-C6 alkyl radical or a halogen, in particular chlorine, Me is a transition metal, in particular zirconium, and Hal is a halogen, in particular chlorine, and a compound, containing aluminum, of the aluminoxane type having the general formulae
Al2OR4(Al(R)—O)n
for a linear aluminoxane and/or
(Al(R)—O)n—2
for a cyclic aluminoxane, in which n is a number from 4 to 20 and R is a methyl or ethyl radical, preferably a methyl radical.
Description
- The present invention relates to a process for the preparation of fulvene-metal complexes, new fulvene-metal complexes and their use as catalysts for the polymerization of unsaturated compounds, in particular for the polymerization and copolymerization of olefins and/or dienes.
- Metal complexes with cyclopentadienyl ligands have been the subject of intense investigation since the discovery of ferrocene. The use of cyclopentadienyl-metal complexes, in particular the use of metallocene complexes as a mixture with activating cocatalysts, preferably alumoxanes, for the polymerization of olefins and diolefins has been known for a long time (e.g. EP-A 69 951, 129 368, 351 392, 485 821, 485 823). Metallocenes have proved to be highly active, specific catalysts in the polymerization of olefins. A large number of new metallocene catalysts and metallocene catalyst systems for the polymerization of olefinic compounds have therefore been developed in recent years in order to increase the activity, selectivity, control of the microstructure, molecular weights and molecular weight distribution.
- Comparatively little is known of metal complexes with fulvene ligands.
- J. Am. Chem. Soc. 1997, 119, 5132 describes zwitter-ionic olefin polymerization catalysts which are formed in the reaction of specific (η6-2,3,4,5-tetramethylcyclopentadienyl-1-methylene) (η5-pentamethylcyclopentadienyl)zirconium compounds with tris(pentafluorophenyl)boron or bispentafluorophenyl)-borane. The synthesis of the (η6-2,3,4,5-tetramethylcyclopentadienyl-1-methylene)(η5-pentamethylcyclopentadienyl)zirconium compound is very expensive, it first being necessary to prepare a metallocene with pentamethylcyclopentadienyl ligands, which is decomposed by a thermolysis reaction in the last synthesis stage. Such thermolysis reactions are described in the literature.
- According to Bercaw et al., JACS (1972), 94, 1219, the fulvene complex (η6-2,3,4,5-tetramethylcyclopentadienyl-1-methylene)(η5-pentamethylcyclopentadienyl)titanium-methyl is formed by thermolysis of bis(η5-pentamethylcyclopentadienyl)titanium-dimethyl. T. J. Marks et al., JACS (1988), 110, 7701 describe the thermolysis of pentamethylcyclopentadienyl complexes of zirconium and hafnium. The fulvene complex (η6-2,3,4,5-tetramethylcyclopentadienyl-1-methylene)η5-pentamethylcyclopentadienyl)zirconium-phenyl is formed by thermnolysis of bis(η5-pentamethylcyclopentadienyl)zirconium-diphenyl.
- The preparation of fulvene complexes by the thermal process is limited to a few structural variants. The thermal process does not always lead to uniform products.
- G. Wilkinson et al. in J. Chem. Soc. 1960, 1321-1324 describe the reaction of 6,6-dialkylfulvenes with chromium-hexacarbonyl or molybdenum-hexacarbonyl. However, cyclopentadienyl-metal complexes are obtained instead of the fulvene-metal complexes.
- In J. Chem. Soc. Dalton Trans. (1985), 2037, M. L. 14. Green et al. report the synthesis of bis(η6-6,6-diphenylfulvene)titanium by reaction of bis(toluene)titanium with 6,6-diphenylfulvene. However, the bis(toluene)titanium must be prepared by involved and expensive metal atom vaporization techniques. For this, metallic titanium is vaporized and condensed in a matrix together with gaseous toluene. The yield of bis(toluene)titanium is very low. The bis(toluene)titanium is therefore accessible to only a limited extent.
- There was therefore the object of discovering an improved process for the preparation of fulvene-metal complexes which avoids the disadvantages mentioned.
- It has now been found, surprisingly, that fulvene-metal complexes can be prepared by reaction of a fulvene compound with a suitable transition metal complex in the presence of a reducing agent.
-
-
- wherein
- M is a metal from group IIIb, IVb, Vb or VIb or the lanthanides or the actinides of the periodic table of the elements according to IUPAC,
- A denotes an anionic ligand optionally with one or more bridges,
- X denotes a hydrogen atom, a C1- to C10-alkyl group, a C1- to C10-alkoxy group, a C6- to C10-aryl group, a C6- to C10-aryloxy group, a C2- to C10-alkenyl group, a C7- to C40-arylalkyl group, a C7-to C40-alkylaryl group, a C8- to C40-arylalkenyl group, a silyl group substituted by C1- to C10-hydrocarbon radicals, a halogen atom or an amide of the formula NR7 2,
- L denotes a neutral ligand,
- R1, R2, R3, R4, R5, R6 are identical or different and represent hydrogen, halogen, a cyano group, a C1- to C20-alkyl group, a C1- to C10-fluoroalkyl group, a C6- to C10-fluoroaryl group, a C1- to C10-alkoxy group, a C6- to C20-aryl group, a C6- to C10-aryloxy group, a C2- to C10-alkenyl group, a C7- to C40-arylalkyl group, a C7- to C40-alkylaryl group, a C1- to C40-arylalkenyl group, a C2- to C10- alkinyl group, a silyl group substituted by C1-C10-hydrocarbon radicals, a sulfide group substituted by a C1-C10-hydrocarbon radical or an amino group which is optionally substituted by C1-C20-hydrocarbon radicals,
- or
- R1, R2, R3, R4, R5, R6, in each case together with the atoms connecting them, form one or more aliphatic or aromatic ring systems, which can contain one or more heteroatoms (O, N, S) and 5 to 10 carbon atoms,
- R7 represents hydrogen, a C1- to C20-alkyl group, a C6- to C20-aryl group, a C7- to C40-arylalkyl group, a C7- to C40-alkylaryl group, a silyl group substituted by C1-C10-hydrocarbon radicals or an amino group which is optionally substituted by C1-C20-hydrocarbon radicals,
- m, p represent the
numbers 0, 1, 2, 3 or 4, which result from the valency and the bonding state of M, and - k represents the number 1, 2 or 3, and the sum of k+m+p is 1 to 5, depending on the oxidation level of M, and
- n is a number from 0 to 10,
- by reaction of a transition metal compound of the formula (IIa) or (IIb)
- AmXsM (IIa)
- or
- AmXsLnM (IIb)
- wherein
- A, X, L, M, m, s and n have the abovementioned meaning and
- s is 2, 3, 4, 5 or 6 and s is >p,
-
- wherein
- R1, R2, R3, R4, R5 and R6 have the abovementioned meaning,
- in the presence of a reducing agent.
-
- The reaction can be carried out in a single reaction step, i.e. in a one-pot reaction, the sequence of addition of the individual reaction components not being fixed. The reaction can also be carried out in separate reaction steps. For example, transition metal compounds of the formula (IIa) or (IIb) can first be brought into contact with a reducing agent and reacted with fulvene compounds of the formula (III) in a separate reaction step. It is furthermore preferable first to add the transition metal compound (IIa) or (IIb) to the fulvene compound (III) and then to add the reducing agent.
- Examples of suitable reducing agents are alkali metals, alkaline earth metals, aluminium, zinc, alloys of the alkali metals, such as e.g. sodium-potassium alloys or sodium amalgam, alloys of the alkaline earth metals, and metal hydrides. Examples of metal hydrides are lithium hydride, sodium hydride, magnesium hydride, aluminium hydride, lithium aluminium hydride and sodium borohydride. Specific examples of reducing agents are sodium naphthalenide, potassium graphite, lithium-alkyls, magnesium-butadiene, magnesium-anthracene, trialkylaluminium compounds and Grignard reagents. Preferred reducing agents are alkali metals or alkaline earth metals, C1-C6-alkyllithium, tri-C1-C6-alkylaluminium compounds and Grignard reagents. Preferred reducing agents are lithium, magnesium, n-butyllithium and triethylaluminium and triisobutylaluminium. Instead of the reducing agents mentioned, it is also possible to carry out an electrochemical reduction.
- The process for the preparation of the fulvene-metal complexes of the formula (I) is carried out in a suitable reaction medium at temperatures of −100 to +250° C., preferably −78 to +130° C., particularly preferably −10 to +120° C.
- Examples of possible suitable reaction media are aliphatic or aromatic hydrocarbons, halogenated hydrocarbons, ethers and cyclic ethers. Examples of these are unbranched aliphatic hydrocarbons, such as butane, pentane, hexane, heptane and octane, branched aliphatic hydrocarbons, such as isobutane, isopentane and isohexane, cyclic aliphatic hydrocarbons, such as cyclohexane and methylcyclohexane, aromatic hydrocarbons, such as benzene, toluene and xylene, and ethers, such as dialkyl ethers, dimethoxyethane and tetrahydrofuran. Mixtures of various solvents are also suitable.
- The fulvene-metal complexes of the formula (I) are prepared and handled with the exclusion of air and water under inert gas conditions (inert gas technique). Examples of inert gases are nitrogen or argon. The Schlenk technique generally conventional for organometallic substances is suitable, for example, as an inert gas technique.
- The fulvene-metal complexes of the formula (I) can be isolated or employed directly for further reactions. If isolation is necessary, the by-products formed can be removed by conventional methods of purification, e.g. by filtration. Alternatively, the desired products can also be extracted with a solvent. If necessary, a purification operation, e.g. recrystallization, can be carried out.
- Possible transition metal complexes of the formula (IIa) or (IIb) are, in particular, those in which
- M is a metal from the group consisting of titanium, zirconium, hafnium, vanadium, niobium, tantalum and chromium,
- A is a pyrazolate of the formula N2C3R8 3 where R8 represents hydrogen or a C1-C10-alkyl group or a C6-C10-aryl group, a pyrazolylborate of the formula R7B(N2C3R8 3)3, an alcoholate or phenolate of the formula OR7, a siloxane of the formula OSiR7 3, a thiolate of the formula SR7, an acetylacetonate of the formula (R7CO)2CR7, a diimine of the formula (R7N═CR7)2, an amidinate of the formula R7C(NR7 2)2, a cyclooctatetraenyl of the formula C8HqR7 8-q where q is 0, 1, 2, 3, 4, 5, 6 or 7, a cyclopentadienyl of the formula C5HqR7 5-q where q is 0, 1, 2, 3, 4 or 5, an indenyl of the formula C9H7-rR7 r where r is 0, 1, 2, 3, 4, 5, 6 or 7, a fluorenyl of the formula C13H9-sR7 s where s is 0, 1, 2, 3, 4, 5, 6, 7, 8 or 9 or a C1- to C30-alkyl radical, a C6- to C10-aryl radical or a C7- to C40-alkylaryl radical and
- L, X, R7, m, s and n have the abovementioned meaning.
- Especially preferred transition metal complexes of the formula (IIa) or (IIb) are those in which
- M represents titanium, zirconium or hafnium,
- A represents bis(trimethylsilyl)amide, dimethylamide, diethylamide, diisopropylamide, 2,6-di-tert-butyl-4-methylphenolate, cyclooctatetraenyl, cyclopentadienyl, methylcyclopentadienyl, benzylcyclopentadienyl, n-propylcyclopentadienyl, n-butylcyclopentadienyl, iso-butylcyclopentadienyl, t-butylcyclopentadienyl, cyclopentylcyclopentadienyl, octadecylcyclopentadienyl, 1,2-dimethylcyclopentadienyl, 1,3-dimethylcyclopentadienyl, 1,3-diisopropylcyclopentadienyl, 1,3-di-t-butylcyclopentadienyl, 1-ethyl-2-methylcyclopentadienyl, 1-isopropyl-3-methylcyclopentadienyl, 1-(n-butyl)-3-methylcyclopentadienyl, 1-(t-butyl)-3-methylcyclopentadienyl, pentamethylcyclopentadienyl, 1,2,3,4-tetramethylcyclopentadienyl, 1,2,4-trimethylcyclopentadienyl, 1,2,4-triisopropylcyclopentadienyl, 1,2,4-tri-(t-butyl)-cyclopentadienyl, indenyl, tetrahydroindenyl, 2-methylindenyl, 4,7-dimethylindenyl, 2-methyl-4,5-benzoindenyl, 2-methyl-4-phenylindenyl, fluorenyl or 9-methylfluorenyl,
- X denotes fluorine or chlorine and
- L, m, s and n have the abovementioned meaning.
- Possible fulvene compounds are, in particular, those of the formula (III) in which
- R1 to R6 represents a C1-C30-alkyl group, a C6-C10-aryl group or a C7-C40-alkylaryl group, in particular hydrogen, methyl, trifluoromethyl, ethyl, n-propyl, isopropyl, n-butyl, isobutyl, tert-butyl, phenyl, pentafluorophenyl, methylphenyl, cyclohexyl or benzyl.
-
-
- wherein
- R1, R2, R3 and R4 have the abovementioned meaning.
- Particularly preferred compounds of the formula (III) are 6-cyclohexylfulvene, 6-isopropylfulvene, 6-tert-butylfulvene, 6-phenylfulvene, 6-(dimethylamino)fulvene, 6,6-bis(dimethylamino)fulvene, 6,6-dimethylfulvene, 6,6-bis(trifluoromothyl)-fulvene, 6,6-diphenylfulvene, 6,6-bis(pentafluorophenyl)fulvene, 6,6-pentamethylenefulvene, 6,6-tetramethylenefulvene, 6,6-trimethylenefulvene, 2-(2,4-cyclopentadien-1-ylidene)-1,3-dithiolane, 5-benzylidene-1,2,3-triphenyl-1,3-cyclopentadiene, 1,2,3,4-tetramethylfulvene, 1,2,3,4-tetraphenylfulvene, 2,3-dimethylfulvene, 2,3-diisopropylfulvene, 2,3-diphenylfulvene, 1,4-dimethyl-2,3-diphenylfulvene and 1,4-diethyl-2,3-diphenylfulvene.
- The synthesis of the fulvene compounds of the formula (III), (IV) and (V) can be carried out, for example, in accordance with the method of J. Org. Chem., Vol. 49, No. 11(1984), 1849.
- The formula (I) given for the fulvene-metal complexes is to be regarded as a formal illustration of the bonding circumstances. The bonding circumstances in the metal complexes depend, inter alia, on the central atom, on the oxidation level and on the substituents of the fulvene ligand.
- FIG. 1 shows in perspective the structure of a fulvene-metal complex which can be prepared according to the invention such as is obtained by X-ray structure analysis, taking the compound (6-tert-butylfulvenyl)pentamethylcyclopentadienyl)titanium chloride as an example.
- The process according to the invention opens up an access to new fulvene-metal complexes of the formula (I) which e.g. cannot be formed by thermolysis.
- The present invention therefore also provides fulvene-metal complexes of the formula (I) in which
- M is a metal from the group consisting of titanium, zirconium, hafnium, vanadium, niobium, tantalum and chromium,
- k is 1 and
- A, X, m, p, R1, R2, R3, R4, R5 and R6 have the abovementioned meaning,
- with the exception of the compounds of the formula (1) wherein
- R1 and R2 represent hydrogen and at the same time R3, R4, R5 and R6 represent a methyl group and at the same time A denotes a pentamethylcyclopentadienyl group or a carboranediyl group of the formula C2B91111.
- The present invention also provides a catalyst system comprising a
- (a) fulvene-metal complex of the formula (I) prepared by the process according to the invention, wherein
- M is a metal from the group consisting of titanium, zirconium, hafnium, vanadium, niobium, tantalum and chromium,
- k is 1 and
- A, X, m, p, R1, R2, R3, R4, R5 and R6 have the abovementioned meaning, and
- (b) a cocatalyst suitable for activating the metal complex (a), the molar ratio of component (a) to component (b) being in the range from 1:0.1 to 1:10,000, preferably 1:1 to 1;1,000.
- Possible cocatalysts are the cocatalysts known in the field of metallocene catalysis, such as polymeric or oligomeric aluminoxanes, Lewis acids and aluminates and borates. In this connection, reference is made in particular to Macromol. Symp. Vol. 97, July 1995, p. 1-246 (for alumoxanes) and to EP 277 003, EP 277 004 and Organometallics 1997, 16, 842-857 (for borates), and EP 573 403 (for aluminates).
- Particularly suitable cocatalysts are methylaluminoxane, methylalumoxane and diisobutylalumoxane modified by triisobutylaluminium, trialkylaluminium compounds, such as trimethylaluminium, triethylaluminium, triisobutylaluminium and trilsooctylaluminium, and furthermore dialkylaluminium compounds, such as diisobutylaluminium hydride, diisobutylaluminium fluoride and diethylaluminium chloride, substituted triarylaluminium compounds, such as tristpentafluorophenyl)aluminium, and ionic compounds which contain tetrakis(pentafluorophenyl)aluminate as the anion, such as triphenylmethyl tetrakis(pentafluorophenyl)aluminate and N,N-dimethylanilinium tetrakis-(pentafluorophenyl)aluminate, substituted triarylboron compounds, such as tris(pentafluorophenyl)boron, and ionic compounds which contain tetrakis(pentafluorophenyl)borate as the anion, such as triphenylmethyl tetrakis(pentafluorophenyl)borate and N,N-dimethylanilinium tetrakis-(pentafluorophenyl)borate. Mixtures of various cocatalysts are also suitable for activation of the fulvene-metal complexes of the formula (I).
- The present invention also provides the use of the new catalyst system for the polymerization of unsaturated compounds, in particular olefins and dienes. Both homopolymerization and copolymerization of the unsaturated compounds mentioned are understood as polymerization here. Compounds which are employed in particular in the polymerization are C2-C10-alkenes, such as ethylene, propylene, but-1-ene, pent-1-ene and hex-1-ene, oct-1-ene and isobutylene, and arylalkenes, such as styrene. Dienes which are employed in particular are: conjugated dienes, such as 1,3-butadiene, isoprene and 1,3-pentadiene, and non-conjugated dienes, such as 1,4-hexadiene, 1,5-heptadiene, 5,7-dimethyl-1,6-octadiene, 4-vinyl-1-cyclohexene, 5-ethylidene-2-norbornene, 5-vinyl-2-norbornene and dicyclopentadiene.
- The catalysts according to the invention are suitable for the preparation of rubbers based on copolymers of ethylene with one or more of the α-olefins mentioned and the dienes mentioned. The catalyst system according to the invention is furthermore suitable for the polymerization of cyclo-olefins, such as norbornene, cyclopentene, cyclohexene and cyclooctene, and the copolymerization of cycloolefins with ethylene or α-olefins.
- The polymerization can be carried out in the liquid phase, in the presence or absence of an inert solvent or in the gas phase. Suitable solvents are aromatic hydrocarbons, such as benzene and/or toluene, or aliphatic hydrocarbons, such as propane, hexane, heptane, octane, isobutane or cyclohexane, or mixtures of the various hydrocarbons.
- It is possible to employ the catalyst system according to the invention applied to a support. Suitable support materials which may be mentioned are e.g.: inorganic or organic polymeric supports, such as silica gel, zeolites, carbon black, active charcoal, aluminium oxide, polystyrene and polypropylene.
- The catalyst system according to the invention can be applied here to the support materials in the conventional manner. Methods of supporting catalyst systems are described, for example, in U.S. Pat. Nos. 4,808,561, 4,912,075, 5,008,228 and 4,914,253.
- The polymerization is in general carried out under pressures of 1 to 1,000, preferably 1 to 100 bar and at temperatures of −100 to +250° C., preferably 0 to +150° C. The polymerization can be carried out continuously or discontinuously in conventional reactors.
- The invention is explained in more detail with the aid of the following examples.
- General information: Organometallic compounds were prepared and handled with the exclusion of air and moisture under argon protection (Schlenk technique). All the solvents required were rendered absolute before use by boiling over a suitable desiccant for several hours and subsequent distillation under argon. The compounds were characterized by1H-NMR, 13C-NMR and mass spectroscopy.
- Abbreviations:
- Cp:cyclopentadienyl
- Cp*:pentamethylcyclopentadienyl
- HV:high vacuum
- RT:room temperature
- THF:tetrahydrofuran
- MS:mass spectrum
- EA:elemental analysis
- Tg:glass transition temperature (DSC measurement)
- de:diastereomer excess
- Fulvene complex synthesis by reaction of 6,6-dimethylfulvene with Cp*TiCl3 in the presence of magnesium [(C5(CH3)5)(C5H4)C(CH3)2TiCl]
- Cp*TiCl3 (0.610 g, 2.11 mmol) and 1.05 equivalents of magnesium (0.054 g, 2.21 mmol) were initially introduced into 25 ml THF. 1.05 equivalents of 6,6-dimethylfulvene (0.227 g, 2.14 mmol) were added dropwise to this mixture at room temperature. The mixture was subsequently stirred overnight at RT so that all the Mg was consumed. The solvent was removed under HV and the green residue was taken up in hexane. The solid was filtered off and the solution was concentrated to half, green shiny platelets precipitating out. For recrystallization, the mixture was cooled to −20° C. The olive-green crystals were isolated and dried under HV. 0.429 g (59%) [(C5(CH3)5)(CH4)C(CH3)2TiCl] was obtained.
-
-
- MS (70 eV) m/e/(%): 324 (40) [M+], 288 (40) [M+—HCl], 135 (5) [Cp*], 106 (100) [dimethylfulvene].
- Fulvene complex synthesis by reaction of 6,6-dimethylfulvene with Cp*TiCl3, in the presence of butyllithium [(Cp*)(C5H4=C(CH3)2)TiCl]400 mg (1.38 mmol) Cp*TiCl3, 154 mg (1.45 mmol) 6,6-dimethylfulvene and 1.11 ml (2.76 mmol) n-butyllithium were combined in 25 ml THF in a Schlenk vessel at a temperature of −78° C. The mixture was allowed to warm slowly to 0° C. and was stirred for a further two hours at this temperature in order to bring the reaction to completion. The solvent was then removed under HV and the green residue was taken up in n-hexane. The solid was filtered off and the solution was concentrated to half, green crystals precipitating out. 290 mg (65%) [(C5(CH3)5)(C5H4)C(CH3)2TiCl] were obtained.
-
-
- Fulvene complex synthesis by reaction of 6,6-dimethylfulvene with Cp*ZrCl3 in the presence of magnesium [(C5(CH3)5)(C5H4)C(CH3)2ZrCl]
- Cp*ZrCl3 (0.380 g, 1.14 mmol) and 1.1 equivalents of magnesium (0.031 g, 1.26mmol) were initially introduced into 10 ml THF. 1.1 equivalents of 6,6-dimethylfulvene (0.134 g, 1.26 mmol) were added dropwise to this solution. After 5 min clouding of the reaction solution occurred. The mixture was stirred overnight so that the magnesium dissolved completely. It was concentrated to dryness under HV, the residue was taken up in 10 ml hexane and the precipitate formed was filtered off. 197 mg (47%) [(C5(CH3)5)(C5H4)C(CH3)2ZrCl] were isolated from the filtrate as a brown-red solid.
-
-
- MS (70 eV) m/e (%): 366 (10) [M+], 330 (5) [M+-HCl], 259 (2), 135 (5) [Cp*], 106 (100) [dimethylfulvene].
- Synthesis of bis(η-6,6-diphenylfulvene)titanium by reaction of 6,6-diphenylfulvene with titanium tetrachloride in the presence of magnesium
- 610 mg (1.83 mmol) TiCl4(THF)2, 89 mg (3.65 mmol) magnesium filings and 841 mg (3.65 mmol) 6,6-diphenylfulvene were combined in 30 ml THF as the reaction medium in a Schlenk vessel. The mixture was stirred for 12 h, until the magnesium filings had been consumed completely, in order to bring the reaction to completion. By concentrating the reaction solution to dryness a green solid was obtained, which could be separated off from the magnesium chloride formed by taking up in n-hexane and filtration. 640 mg (70%) bis(η6-6,6-diphenylfulvene)titanium were obtained by stepwise concentration and cooling of the filtrate.
- Fulvene complex synthesis by reaction of 6,6-dimethylfulvene with CpTiCl3 in the presence of magnesium [(C5H5)(C5H4)C(CH3)2TiCl]
- CpTCl3 (0.410 g, 1.87 mmol) and 1.05 equivalents of magnesium (0.048 g, 1.96 mmol) were initially introduced into 20 ml THF. 1.03 equivalents of 6,6-dimethylfulvene (0.204 g, 1.92 mmol) were added dropwise to this yellow solution at RT and the mixture was stirred until the magnesium employed had been consumed. It was then concentrated under HV and the resulting green solid was taken up in 20 ml hexane. After the solid had been filtered off, the dark green solution was concentrated to half under HV. 0.2 g (42%) [(C5H5(C5H4)C(CH3)2TiCl] was obtained as a dark green solid by crystallization at −20° C.
-
-
- Fulvene complex synthesis by reaction of 6,6-diphenylfulvene with Cp*TiCl3 in the presence of magnesium [(C5(CH3)5)(C5,H4)C(C6H5)2TiCl]
- Cp*TiCl3 (0.690 g, 2.38 mmol) and 1.1 equivalents of magnesium (0.064 g, 2.62 mmol) were initially introduced into 20 ml THF. 1.1 equivalents of 6,6-diphenylfulvene (0.604 g, 2.62 mmol) were added dropwise to this solution at RT. The mixture was stirred overnight at RT, so that all the magnesium was consumed. The solvent was removed under HV and the green residue was taken up in hexane. The precipitate was filtered off and the solution was concentrated to half. The mixture was cooled to −20° C. for crystallization, 0.29 g (27%) [(C5(CH3)5)(C5H4)C(C6H5)2TiCl] being obtained as a green solid.
-
-
- MS (70 eV) m/e (%): 448 (5) [M+], 413 (2) [M+-HCl], 230 (100) [6,6-diphenylfulvene], 135 (15) [Cp*], 78 (12) [Ph].
- Fulvene complex synthesis by reaction of 6,6-diphenylfulvene with Cp*ZrCl3 in the presence of magnesium [(C5(CH3)5)(C5H4)C(C6H5)2ZrCl]
- Cp*ZrCl3 (0.310 g, 0.93 mmol) and 1.05 equivalents of magnesium (0.024 g, 0.98 mmol) were initially introduced into 10 ml THF. 1.05 equivalents of 6,6-diphenylfulvene (0.225 g, 0.98 mmol) were added dropwise to this solution. The mixture was stirred overnight, so that the magnesium had reacted completely. It was concentrated to dryness under HV, the residue was taken up in 20 ml toluene and the insoluble precipitate was filtered off. After covering with a layer of hexane at −20° C., 178 mg (39%) [(C5(CH3)5)(C5H4)C(C6H5)2ZrCl] were obtained as a red solid.
-
-
- MS (70 eV) m/e (%): 448 (5) [M+], 413 (2) [M+-HCl], 230 (100) [6,6-diphenylfulvene], 135 (15) [Cp*], 78 (12) [Ph].
- Fulvene complex synthesis by reaction of 2,3,4,5-tetramethylfulvene with Cp*TiCl3 in the presence of magnesium [(C5(CH3)5)(C5(CH3)4)CH2TiCl]
- Cp*TiCl3 (0.370 g, 1.28 mmol) and 1.05 equivalents of magnesium (0.033 g, 1.35 mmol) were initially introduced into 25 ml THF. 1.05
equivalents 2,3,4,5-tetramethylfulvene (0.185 g, 1.35 mmol) were added dropwise to this red solution at room temperature. The mixture was stirred overnight at RT so that all the magnesium was consumed. The solvent was removed under HV and the green residue was taken up in hexane. The solid was filtered off and the solution was concentrated to half. The mixture was cooled to −20° C. for crystallization, 0.23 g (52%) [(C5(CH3)5)(C5(CH3)4)CH2TiCl] being obtained as a green solid. -
-
- Fulvene complex synthesis by reaction of 2,3,4,5-tetramethylfulvene with CpTiCl3 in the presence of magnesium [(C5H5)C5(CH3)4)CH2TiCl]
- CpTiCl3 (0.350 g, 1.60 mmol) and 1.05 equivalents of magnesium (0.041 g, 1.67 mmol) were initially introduced into 20 ml THF. 1.1 equivalents of 2,3,4,5-tetramethylfulvene (0.260 g, 1.67 mmol) were added dropwise to this solution at room temperature and the mixture was stirred until the magnesium employed had been consumed. It was then concentrated under HV and the resulting green solid was taken up in 20 ml hexane. After the solid had been filtered off, the dark green solution was concentrated to half under HV. 0.3 g (67%) [(C5H5)C5(CH3)4)CH2TiCl] was obtained as a dark green solid by crystallization at −20° C.
-
-
- MS (70 eV) m/e (%): 283 (10) [M+], 247 (15) [M+—HCl], 134 (50) [2,3,4,5-tetramethylfulvene], 119 (100) [2,3,4,5-tetramethylfulvene-CH4], 65 (30) [Cp].
- Fulvene complex synthesis by reaction of 1,2,3,4,6-pentamethylfulvene with CpTiCl3 in the presence of magnesium [(C5H5)(C5(CH3)4C(H)(CH3)TiCl]
- CpTiCl3 (0.450 g, 2.05 mmol) and 1.05 equivalents of magnesium (0.054 g, 2.15 mmol) were initially introduced into 20 ml THF. 1.03 equivalents of 1,2,3,4,6-pentamethylfulvene (0.320 g, 2.15 mmol) were added dropwise to this solution at RT and the mixture was stirred until the magnesium employed had been consumed. It was then concentrated under HV and the resulting green solid was taken up in 20 ml hexane. After the solid had been filtered off, the dark green solution was concentrated to half under HV. 0.17 g (28%) [(C5H5)(C5(CH3)4)C(H)(CH3)TiCl] was obtained as a dark green solid by crystallization at −20° C.
- de: 25%
-
-
- Fulvene complex synthesis by reaction of 6-tert-butylfulvene with Cp*TiCl3 in the presence of magnesium [(C5(CH3)5)(C5H4)C(H)(C(CH3)3)TiCl]
- Cp*TiCl3 (0.450 g, 1.55 mmol) and 1.05 equivalents of magnesium (0.039 g, 1.63 mmol) were initially introduced into 15 ml THF. 1.05 equivalents of tertbutylfulvene (0.249 g, 1.63 mmol) were added dropwise to this solution at RT. The mixture was stirred overnight at RT so that all the magnesium was consumed. The solvent was removed under HV and the green residue was taken up in hexane. The solid was filtered off and the solution was concentrated to half. The mixture was cooled to −20° C. for crystallization, 0.35 g (64%) [(C5(CH3)5)(C5H4)C(H)-(C(CH3)3)TiCl] being obtained as green crystals.
- An X-ray structure analysis was carried out (FIG. 1).
- de: ≧98%
-
-
- MS (70 eV) m/e (%): 353 (12) [M+], 316 (5) [M+-HCl], 270 (18), 235 (8), 135 (100) [Cp*], 119 (35), 80 (85), 57 (90) [C(CH3)3].
- Fulvene complex synthesis by reaction of 6-tert-butylfulvene with CpTCl3 in the presence of magnesium [(C5H5)(C5H4)C(H)(C(CH3)3)TiCl]
- CpTiCl3 (0.420 g, 1.91 mmol) and 1.05 equivalents of magnesium (0.048 g, 2.01 mmol) were initially introduced into 10 ml THF. 1.03 equivalents of tertbutylfulvene (0.295 g, 1.91 mmol) were added dropwise to this solution at RT and the mixture was stirred under the magnesium employed was consumed. It was then concentrated under HV and the resulting green solid was taken up in 20 ml hexane. After the solid had been filtered off, the dark green solution was concentrated to half under HV. 0.23 g (44%) [(C5H5)(C5H4)C(H)(C(CH3)3)TiCl] was obtained as dark green crystals by crystallization at −20° C.
- de: ≧98%
-
-
- MS (70 eV) m/e (%): 282 (5) [M+], 246 (45) [M+—HCl], 228 (15), 135 (10) [Cp*], 119 (35).
- Preparation of the catalyst solution
- 8.3 mg (22.6 μmol) [(Cp*)(C5H4=C(CH3)2)ZrCl] from example 3 were dissolved in 11.3 ml toluene.
- Polymerization of ethylene
- 100 ml toluene were initially introduced into a 250 ml glass reactor and 1 ml of a 0.1 molar solution of triisobutylaluminium in toluene and 0.5 ml of the catalyst solution were added. Ethylene was then passed continuously into the solution under a pressure of 1.1 bar with a gas inlet tube. The polymerization was initiated by addition of 1 ml of a 0.001 molar solution of N,N-dimethylanilinium tetrakis(pentafluorophenyl)borate in toluene. After a polymerization time of 5 min at a temperature of 40° C. under an ethylene pressure of 1.1 bar, the reaction was stopped by addition of 10 ml methanol and the polymer formed was filtered off, washed with acetone and dried in a vacuum drying cabinet. 1.61 g polyethylene were obtained.
- Copolymerization of ethylene and propylene
- 500 ml toluene and 5 ml of a 10% MAO solution in toluene were initially introduced into a 1.4 l steel autoclave, equipped with a mechanical stirrer, manometer, temperature probe, temperature control device, catalyst sluice and monomer metering devices for ethylene and propylene, and were stirred for 10 min. 52 g propylene were then metered in. The internal temperature was adjusted to 40° C. with a thermostat. Ethylene was then metered in until the internal pressure in the reactor rose to 6 bar. The polymerization was initiated by addition of 5 ml of the catalyst solution from example 5 and ethylene was metered in continuously such that the internal pressure at 40° C. was constant at 6 bar. After a polymerization time of 1 hour the polymerization was stopped with a 1% HCl solution in methanol, the mixture was stirred for 10 min and the polymer was then precipitated in methanol. The polymer thus obtained was washed with methanol, isolated and dried in vacuo at 60° C. for 20 h, 48 g copolymer being obtained. Determination of the composition of the copolymer by IR spectroscopy showed an incorporation of 82.9% ethylene and 17.1% propylene. A Tg of −24° C. was determined by the DSC method.
- Preparation of the catalyst
- 73.9 mg (0.221 mmol) TiCl4(THF)2 were dissolved in 3 ml THF. 5.4 mg (0.22 mmol) magnesium and 51 mg (0.221 mmol) 6,6-diphenylfulvene were then added. After stirring at 20° C. for 20 h, a dark green solution was obtained. The solution was concentrated to dryness, the residue formed was dried under HV for 2 h and 22 ml toluene were then added, a dark green suspension being formed. 1 ml of the catalyst suspension contained 0.01 mmol titanium.
- Polymerization of ethylene
- 90 ml toluene and 5 ml of an MAO solution (10% in toluene) were initially introduced into a 250 ml glass reactor and were stirred for 5 minutes. 5 ml of the catalyst suspension were then added and the mixture was stirred at 40° C. for 10 minutes. Ethylene was then passed continuously into the solution with a gas inlet tube. After a polymerization time of 10 min at a temperature of 40° C. and an ethylene pressure of 1.1 bar, the reaction was stopped by addition of 10 ml of a 1% solution of HCl in methanol and the polymer formed was filtered off, washed with methanol and dried in a vacuum drying cabinet. 8.9 g polyethylene were obtained.
Claims (8)
1. Process for the preparation of fulvene-metal complexes of the formula (Ia)
or of the formula (Ib)
wherein
M is a metal from group IIIb, IVb, Vb or VIb or the lanthanides or the actinides of the periodic table of the elements according to IUPAC,
A denotes an anionic ligand optionally with one or more bridges,
X denotes a hydrogen atom, a C1- to C10-alkyl group, a C1- to C10-alkoxy group, a C6- to C10-aryl group, a C6- to C10-aryloxy group, a C2- to C10-alkenyl group, a C7- to C40-arylalkyl group, a C7-to C40-alkylaryl group, a C8- to C40-arylalkenyl group, a silyl group substituted by C1- to C10-hydrocarbon radicals, a halogen atom or an amide of the formula NR7 2,
L denotes a neutral ligand,
R1, R2, R3, R4, R5, R6 are identical or different and represent hydrogen, halogen, a cyano group, a C1- to C20-alkyl group, a C1- to C10-fluoroalkyl group, a C6- to C10-fluoroaryl group, a C1- to C10-alkoxy group, a C6- to C20-aryl group, a C6- to C10-aryloxy group, a C2- to C10-alkenyl group, a C7- to C40-arylalkyl group, a C7- to C40-alkylaryl group, a C8- to C40-arylalkenyl group, a C2- to C10-alkinyl group, a silyl group substituted by C1-C10-hydrocarbon radicals, a sulfide group substituted by a C1-C10-hydrocarbon radical or an amino group which is optionally substituted by C1-C20-hydrocarbon radicals,
or
R1, R2, R3, R4, R5, R6, in each case together with the atoms connecting them, form one or more aliphatic or aromatic ring systems, which can contain one or more hetero atoms (O, N, S) and 5 to 10 carbon atoms,
R7 represents hydrogen, a C1- to C20-alkyl group, a C6- to C20-aryl group, a C7- to C40-arylalkyl group, a C1- to C40-alkylaryl group, a silyl group substituted by C1-C10-hydrocarbon radicals or an amino group which is optionally substituted by C1-C20-hydrocarbon radicals,
m, p represent the numbers 0, 1, 2, 3 or 4, which result from the valency and the bonding state of M, and
k represents the number 1, 2 or 3, and the sum of k+m+p is 1 to 5, depending on the oxidation level of M, and
n is a number from 0 to 10,
by reaction of a transition metal compound of the formula (IIa) or (IIb)
AmXsM (IIa)
or
AmXsLnM (IIb)
wherein
A, X, L, M, m, s and n have the abovementioned meaning and
s is 2, 3, 4, 5 or 6 and s is >p,
with a fulvene compound of the formula (III)
wherein
R1, R2, R3, R4, R5 and R6 have the abovementioned meaning,
in the presence of a reducing agent.
2. Process according to claim 1 , characterized in that the reaction is carried out in a suitable reaction medium at temperatures of −100 to +250° C.
3. Process according to claim 1 , characterized in that alkali metals, alkaline earth metals or lithium-alkyls are used as the reducing agent.
4. Process according to claim 1 , characterized in that the reaction is carried out in a solvent.
5. Process according to claim 4 , characterized in that the reaction is carried out in an ether.
6. Fulvene-metal complexes of the formula (Ia) or (Ib), wherein
M is a metal from the group consisting of titanium, zirconium, hafnium, vanadium, niobium, tantalum and chromium,
k is 1 and
A, X, L, m, n, p, R1, R2, R3, R4, R5 and R6 have the abovementioned meaning,
with the exception of the compounds of the formula (Ia) or (Ib) wherein
R1 and R2 represent hydrogen and at the same time R3, R, R5 and R6 represent a methyl group and at the same time A denotes a pentamethylcyclopentadienyl group or a carboranediyl group of the formula C2B91111.
7. Catalyst system comprising:
(a) a fulvene-metal complex of the formula (Ia) or (Ib) prepared by the process according to claim 1 , wherein
M is a metal from the group consisting of titanium, zirconium, hafnium, vanadium, niobium, tantalum and chromium,
k is 1 and
A, X, L, m, n, p, R1, R2, R3, R4, R5 and R6 have the abovementioned meaning,
and
(b) a cocatalyst suitable for activating the metal complex (a), the molar ratio of component (a) to component (b) being in the range from 1:0.1 to 1:10,000.
8. Use of the catalyst system according to claim 7 for the polymerization of olefins and/or dienes.
Priority Applications (1)
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US09/922,365 US20020010084A1 (en) | 1997-11-07 | 2001-08-03 | Method for producting fulvene metal complexes |
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DE19749293 | 1997-11-07 | ||
DE19749'293.2 | 1997-11-07 | ||
DE19756742A DE19756742A1 (en) | 1997-11-07 | 1997-12-19 | Process for the production of fulven metal complexes |
DE19756742.8 | 1997-12-19 | ||
US09/530,812 US6403735B1 (en) | 1997-11-07 | 1998-10-28 | Method for producing fulvene metal complexes |
US09/922,365 US20020010084A1 (en) | 1997-11-07 | 2001-08-03 | Method for producting fulvene metal complexes |
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EP (1) | EP1028968A1 (en) |
JP (1) | JP2001522856A (en) |
CN (1) | CN1278265A (en) |
AU (1) | AU2047999A (en) |
BR (1) | BR9813196A (en) |
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Cited By (2)
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AU2005220172B2 (en) * | 2004-10-08 | 2011-04-14 | Patria Aerostructures Oy | Pivoting panel for aircraft, and composite support piece |
US20160306044A1 (en) * | 2014-08-11 | 2016-10-20 | Gerard Dirk Smits | Three-dimensional triangulation and time-of-flight based tracking systems and methods |
Families Citing this family (11)
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US6087515A (en) * | 1998-10-07 | 2000-07-11 | Solvay Polyolefins Europe-Belgium (Societe Anonyme) | Metallocenes and process for the preparation of metallocenes |
DE19850898A1 (en) * | 1998-11-05 | 2000-05-11 | Bayer Ag | Process for the preparation of EP (D) M |
DE19924176A1 (en) * | 1999-05-27 | 2000-11-30 | Bayer Ag | Catalyst system based on fulvene compounds |
KR100515585B1 (en) * | 2002-08-29 | 2005-09-16 | 주식회사 엘지화학 | Fulvene-based compound and method for preparing thereof |
CA2464518A1 (en) * | 2002-08-29 | 2004-03-11 | Lg Chem, Ltd. | Fulvene, metallocene catalysts and preparation method thereof, and preparation of polyolefines copolymer using the same |
US7816550B2 (en) * | 2005-02-10 | 2010-10-19 | Praxair Technology, Inc. | Processes for the production of organometallic compounds |
EP2019111A1 (en) * | 2007-07-24 | 2009-01-28 | Total Petrochemicals Research Feluy | Catalyst components based on fulvene complexes |
US8440772B2 (en) * | 2011-04-28 | 2013-05-14 | Chevron Phillips Chemical Company Lp | Methods for terminating olefin polymerizations |
US10273315B2 (en) | 2012-06-20 | 2019-04-30 | Chevron Phillips Chemical Company Lp | Methods for terminating olefin polymerizations |
KR102251989B1 (en) | 2014-03-10 | 2021-05-14 | 삼성전자주식회사 | Organometallic precursors and methods of forming a thin layer using the same |
BR112017017069B1 (en) * | 2015-02-10 | 2021-09-28 | Milliken & Company | HETEROPHASIC POLYMER COMPOSITION |
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DE3127133A1 (en) | 1981-07-09 | 1983-01-27 | Hoechst Ag, 6000 Frankfurt | METHOD FOR PRODUCING POLYOLEFINS AND THEIR COPOLYMERISATS |
US5324800A (en) | 1983-06-06 | 1994-06-28 | Exxon Chemical Patents Inc. | Process and catalyst for polyolefin density and molecular weight control |
US5580939A (en) | 1983-06-06 | 1996-12-03 | Exxon Chemical Patents Inc. | Process and catalyst for polyolefin density and molecular weight control |
US4808561A (en) | 1985-06-21 | 1989-02-28 | Exxon Chemical Patents Inc. | Supported polymerization catalyst |
PL276385A1 (en) | 1987-01-30 | 1989-07-24 | Exxon Chemical Patents Inc | Method for polymerization of olefines,diolefins and acetylene unsaturated compounds |
IL85097A (en) | 1987-01-30 | 1992-02-16 | Exxon Chemical Patents Inc | Catalysts based on derivatives of a bis(cyclopentadienyl)group ivb metal compound,their preparation and their use in polymerization processes |
US4912075A (en) | 1987-12-17 | 1990-03-27 | Exxon Chemical Patents Inc. | Method for preparing a supported metallocene-alumoxane catalyst for gas phase polymerization |
US5008228A (en) | 1988-03-29 | 1991-04-16 | Exxon Chemical Patents Inc. | Method for preparing a silica gel supported metallocene-alumoxane catalyst |
US4892851A (en) | 1988-07-15 | 1990-01-09 | Fina Technology, Inc. | Process and catalyst for producing syndiotactic polyolefins |
US4914253A (en) | 1988-11-04 | 1990-04-03 | Exxon Chemical Patents Inc. | Method for preparing polyethylene wax by gas phase polymerization |
ES2090209T3 (en) | 1990-11-12 | 1996-10-16 | Hoechst Ag | METALLOCENES WITH LIGANDS BASED ON SUBSTITUTED INDENYL DERIVATIVES IN POSITION 2, PROCEDURE FOR THEIR PREPARATION AND USE AS CATALYSTS. |
ES2071888T3 (en) | 1990-11-12 | 1995-07-01 | Hoechst Ag | BISINDENILMETALOCENOS SUBSTITUTED IN POSITION 2, PROCEDURE FOR ITS PREPARATION AND USE AS CATALYSTS IN THE POLYMERIZATION OF OLEFINS. |
US6054405A (en) * | 1997-12-29 | 2000-04-25 | Union Carbide Chemicals & Plastics Technology Corporation | Catalyst composition for the polymerization of olefins |
-
1998
- 1998-10-28 BR BR9813196-6A patent/BR9813196A/en not_active IP Right Cessation
- 1998-10-28 WO PCT/EP1998/006821 patent/WO1999024445A1/en not_active Application Discontinuation
- 1998-10-28 JP JP2000520454A patent/JP2001522856A/en active Pending
- 1998-10-28 EP EP98965145A patent/EP1028968A1/en not_active Withdrawn
- 1998-10-28 CA CA002309174A patent/CA2309174A1/en not_active Abandoned
- 1998-10-28 AU AU20479/99A patent/AU2047999A/en not_active Abandoned
- 1998-10-28 US US09/530,812 patent/US6403735B1/en not_active Expired - Fee Related
- 1998-10-28 CN CN98810873.9A patent/CN1278265A/en active Pending
-
2000
- 2000-05-02 NO NO20002319A patent/NO20002319L/en not_active Application Discontinuation
-
2001
- 2001-08-03 US US09/922,365 patent/US20020010084A1/en not_active Abandoned
Cited By (2)
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AU2005220172B2 (en) * | 2004-10-08 | 2011-04-14 | Patria Aerostructures Oy | Pivoting panel for aircraft, and composite support piece |
US20160306044A1 (en) * | 2014-08-11 | 2016-10-20 | Gerard Dirk Smits | Three-dimensional triangulation and time-of-flight based tracking systems and methods |
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AU2047999A (en) | 1999-05-31 |
JP2001522856A (en) | 2001-11-20 |
US6403735B1 (en) | 2002-06-11 |
EP1028968A1 (en) | 2000-08-23 |
NO20002319D0 (en) | 2000-05-02 |
CA2309174A1 (en) | 1999-05-20 |
WO1999024445A1 (en) | 1999-05-20 |
BR9813196A (en) | 2000-08-29 |
NO20002319L (en) | 2000-06-29 |
CN1278265A (en) | 2000-12-27 |
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