WO1994011406A1 - Indenyl compounds and catalyst components for the polymerization of olefins - Google Patents

Indenyl compounds and catalyst components for the polymerization of olefins Download PDF

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Publication number
WO1994011406A1
WO1994011406A1 PCT/NL1993/000229 NL9300229W WO9411406A1 WO 1994011406 A1 WO1994011406 A1 WO 1994011406A1 NL 9300229 W NL9300229 W NL 9300229W WO 9411406 A1 WO9411406 A1 WO 9411406A1
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Prior art keywords
group
indenyl
grams
polymerisation
ethylene
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PCT/NL1993/000229
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French (fr)
Inventor
Johannus Antonius Maria Van Beek
Johannes Gerardus De Vries
Henricus Johannes Arts
Radjindrakumar Persad
Gerardus Henricus Josephus Van Doremaele
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Dsm N.V.
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Application filed by Dsm N.V. filed Critical Dsm N.V.
Priority to DE69333114T priority Critical patent/DE69333114T2/en
Priority to JP51194394A priority patent/JP3419456B2/en
Priority to RU95112455A priority patent/RU2128183C1/en
Priority to EP94901064A priority patent/EP0668865B1/en
Priority to AU55774/94A priority patent/AU677026B2/en
Priority to BR9307420-4A priority patent/BR9307420A/en
Publication of WO1994011406A1 publication Critical patent/WO1994011406A1/en
Priority to NO951848A priority patent/NO306782B1/en
Priority to FI952266A priority patent/FI114798B/en
Priority to US08/812,675 priority patent/US5990253A/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F210/00Copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F210/16Copolymers of ethene with alpha-alkenes, e.g. EP rubbers
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07FACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
    • C07F17/00Metallocenes
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F10/00Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F10/02Ethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F110/00Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
    • C08F110/02Ethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44Metals; 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
    • C08F4/60Metals; 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
    • C08F4/62Refractory metals or compounds thereof
    • C08F4/639Component covered by group C08F4/62 containing a transition metal-carbon bond
    • C08F4/63912Component covered by group C08F4/62 containing a transition metal-carbon bond in combination with an organoaluminium compound
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08FMACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
    • C08F4/00Polymerisation catalysts
    • C08F4/42Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
    • C08F4/44Metals; 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
    • C08F4/60Metals; 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
    • C08F4/62Refractory metals or compounds thereof
    • C08F4/639Component covered by group C08F4/62 containing a transition metal-carbon bond
    • C08F4/6392Component covered by group C08F4/62 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring
    • C08F4/63922Component covered by group C08F4/62 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring containing at least two cyclopentadienyl rings, fused or not
    • YGENERAL 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S526/00Synthetic resins or natural rubbers -- part of the class 520 series
    • Y10S526/943Polymerization with metallocene catalysts

Definitions

  • the invention relates to indenyl compounds that 10 can be used as catalyst component for the polymerisation of olefins.
  • the invention also relates to a process for the polymerisation of olefins and to a polyolefin.
  • Indenyl compounds are known as catalyst component for olefin polymerisation.
  • the catalysts 15 obtained using indenyl compounds exhibit a high polymerisation activity. See for example DE-A-3,840,772.
  • the known indenyl compounds have the general formula:
  • R' a substituent, other than hydrogen, to the Ind group, 25 Cp a cyclopentadienyl group,
  • M a transition metal from group 3, 4, 5 or 6 of the Periodic System of Elements, 0 a ligand to M.
  • Periodic System of Elements is understood to be the new IUPAC version as printed on the inside cover of the Handbook of Chemistry and Physics, 70th edition, CRC Press, 1989-1990.
  • k is an integer linked to the
  • k equals the valence of M minus two divided by the valence of the 0 group.
  • the Ind group and the Cp group are both bound to the metal M.
  • the said compounds are regarded as belonging to the metallocene compounds (metallocenes).
  • One of the aims of the invention is to provide new indenyl compounds with the general formula (1).
  • Another aim is to provide an indenyl compound having favourable properties as a catalyst component in olefin polymerisation.
  • the invention concerns an indenyl compound having the general formula (1), characterized in that the substituent R' in formula (1) is bound to the Ind group at the 2-position.
  • 2-indenyl compound (2-Ind) In the known indenyl compounds the substituent R' is bound to the I m ⁇ position of the indenyl ring; the known indenyl compounds are therefore 1-indenyl compounds.
  • 2-indenyl compounds were found to exhibit an activity different from that of the known 1-indenyl compounds in olefin polymerisation.
  • solution polymerisation of olefins in particular in the polymerisation to polyethylene, such compounds exhibit higher activity.
  • EA(D)M rubbers ethylene- ⁇ -alkene- (third monomer) rubbers
  • the Cp group in formula (1) is a cyclopentadienyl group or a derivative thereof, like for example a fluorenyl group or an indenyl group, all of them whether or not substituted.
  • EP-A-485,821 and EP-A-485,823 bisindenyl- metallocenes are known having a bridge coupled to the I m ⁇ positions of the indenylgroups. Such metallocenes are expressly excluded.
  • EP-A-372,414 indicates two specific halogenated, bridged metallocenes.
  • the chemical names of the two metallocenes are: ethylene-1-(3-but-3-enyl)inden-1-yl)-2-( (1-but- 3-enyl)-inden-2-yl)zirconiumdichloride, and ethylene-l-( (3-allyldimethylsilyl)-inden-l-yl)- 2-( (1-allyldimethylsilyl)-inden-2-yl)zirconium- dichloride.
  • these two bisindenyl compounds are expressly excluded from the 2-indenyls of the invention.
  • heteroatom containing group examples include: alkylsulphides (like MeS-, PhS-, n-butyl-S-), amines (like Me 2 N-, n-butyl-N-), Si or B containing groups (like Me 3 Si- or Et 2 B-) or P-containing groups (like Me 2 P- or Ph 2 P-). Hydrogenated forms of 2-indenyl compounds also fall within the spirit of the invention.
  • R ' is a hydrocarbon group
  • R ' is preferably an alkyl group, more in particular an alkyl group with 1-4 carbon atoms.
  • the 0 group in the compounds according to the invention comprises one or more uni- or polyvalent anionic ligands to the transition metal.
  • ligands which may be the same or different, the following can be mentioned: a hydrogen atom, a halogen atom, an alkyl group, an aryl group, an aralkyl group, an alkoxy group, an aryloxy group, a group with a heteroatom chosen from group 14, 15 or 16 of the Periodic System of Elements, such as
  • an S compound such as sulphide, sulphite, sulphate, thiol, sulphinate,
  • the number of 0 groups in the 2-indenyl compound according to the invention is determined by the valence of the transition metal M and the valence of the Q groups itself.
  • the transition metal in the 2-indenyl compound (the M group) is chosen from groups 3 through 6 of the Periodic System of Elements.
  • the transition metal is preferably chosen from the group Ti, Zr, Hf, V, Nb, Cr, Ta, Sm and Mo. Zr, Hf or Ti are greatly preferred.
  • Another preferred embodiment of the invention is formed by compounds in which the Cp group is a 2-indenyl group with the formula:
  • R" is a substituent other than hydrogen at the 2- position of the Ind group.
  • R" group a hydrocarbon group (like alkyl, aryl, aralkyl) or a group with at least one heteroatom from group 14, 15 or 16 of the Periodic System of Elements may be used. Such a substituent can be the same as or different from the substituent used as R'.
  • the R" group when being a hydrocarbon group, is preferably an alkyl group, in particular an alkyl group with 1-4 carbon atoms.
  • the indenyl group of formula (1) is a group in which is R' is linked to the Cp group in formula (1).
  • These compounds, in which Rl forms a bridge between the 2- position of the Ind group and the Cp group in formula (1), are referred to as bridged 2-indenyl compounds according to the invention.
  • the other compounds according to formula (1), without the bridge between the 2-indenyl group and the Cp group, are referred to as unbridged 2-indenyl compounds.
  • the Cp group in formula (1) is a 2-indenyl group as well, which is bound to the R' group at the 2-position.
  • bridged bis(2-indenyl) compounds Such compounds according to the invention are referred to as bridged bis(2-indenyl) compounds; in such a case the ' group forms a bridge between two 2-indenyl groups, hence the term bridged bis(2-indenyl) compound.
  • the formula of these bridged bis(2-indenyl) compounds according to the invention may be represented as follows:
  • R is a group derived from R'.
  • R can be chosen to be a hydrocarbon group (like an alkenyl group, an arylalkenyl group) or a group with at least one heteroatom from group 14, 15 or 16 of the Periodic System of Elements.
  • the choice of the R group, when being a hydrocarbon group is between a methylydene group and an ethylydene group.
  • the hydrocarbon groups in these R-groups containing a heteroatom may be varied and can be an alkyl, aryl or aralkylgroup.
  • the 2-indenyl compounds according to the invention can be prepared via different synthesis routes, consisting of synthesis steps known as such. They can for example be prepared by converting a 2-indene compound into its anion.
  • Organolithium, organomagnesium and organosodium compounds can for example be used for this purpose, but also sodium or calcium.
  • organolithium compounds are highly suitable, preferably methyl-lithium or n-butyl-lithium.
  • transition metal compounds that are suitable for trans- metalation are TiCl 4 , ZrCl 4 , HfCl 4 , Zr(OBu) 4 and Zr(OBu) 2 Cl 2 .
  • the trans-metalation is preferably carried out as in NL-A-91,011,502, in a solvent or in a combination of solvents that weakly coordinate to transition metals from the groups 3, 4, 5 or 6 with at most 1 mole equivalent, relative to the transition metal compound started from, of a Lewis base of which the conjugated acid has a pK a greater than -2.5.
  • solvents/dispersants pK a of conjugated acid ⁇ -2.5
  • suitable solvents/dispersants pK a of conjugated acid ⁇ -2.5
  • ethoxyethane dimethoxyethane
  • isopropoxyisopropane n- propoxy-n-propane
  • methoxybenzene methoxymethane
  • n- butoxy-n-butane methoxy-n-butane
  • dioxane Part of the reaction medium may consist of hydrocarbons (hexane and the like).
  • LiCl is formed besides the metallocene. This usually precipitates in the dispersants used.
  • the combination of metallocene and LiCl as such can be used with a co-catalyst (aluminium compound or cation- generating agent) for the polymerisation of olefins.
  • the LiCl may also be separated from the metallocene, for example by dissolving the metallocene in dichloromethane and filtering LiCl off. If the metallocene dissolves in the solvent used in the synthesis, the LiCl can be separated at once by filtration.
  • the 2-indene compounds mentioned heretofore as compounds started from can be formed from commercially available compounds, via synthess routes consisting of several reaction steps known per se.
  • the synthesis route is chosen on the basis of the 2-indenyl compound desired.
  • the unbridged 2-indenyl compounds for example, can be prepared from 2-indanones, which are commercially available, via reaction with an alkyl magnesium halide-, followed by dehydration.
  • the synthesis of the bridged 2- indenyl compounds strongly depends on the 2-indenyl compound desired.
  • Various synthesis routes are described in the examples given hereafter.
  • the 2-indenyl compounds according to the invention can be used, via methods known for metallocenes, as catalyst component for the polymerisation of one or more olefins.
  • the olefin(s) is/are chosen from the group comprising ⁇ -olefins, internal olefins and diolefins. Mixtures of these can also be used.
  • the invention relates in particular to a process for the polymerisation of (an) ⁇ -olefin(s).
  • the ⁇ -olefin(s) is/are preferably chosen from the group comprising ethylene, propylene, butene, pentene, heptene and octene, while mixtures can also be used. More preferably, ethylene and/or propylene is/are used as ⁇ -olefin.
  • the use of such olefins leads to the formation of crystalline polyethylene homopolymers and copolymers of both low and high density (HDPE, LDPE, LLDPE, etc.), and polypropylene homopolymers and copolymers (PP and EMPP).
  • the monomers needed fur such products and the processes to be used are known to the skilled in the art.
  • the process according to the invention is also eminently suitable for the preparation of amorphous or rubbery copolymers based on ethylene and another ⁇ -olefin.
  • Propylene is preferably used as the other ⁇ -olefin, so that EPM rubber is formed.
  • EADM rubber is formed, in particular EPDM (ethylene propylene diene rubber).
  • the 2-indenyl compounds according to the invention can be used as catalyst, both supported and unsupported.
  • the supported catalysts are mainly used in gas-phase and slurry processes.
  • the support is any support known as support for metallocene catalysts, for example Si0 2 or A1 2 0 3 .
  • the 2-indenyl compounds according to the invention are particularly suitable for use as unsupported catalyst in solution polymerisation processes.
  • the known solvents may be used.
  • aliphatic hydrocarbons such as hexane and heptane, and mixtures of aliphatic hydrocarbons are used.
  • the solvent may still contain small amounts of aromatic hydrocarbon, for example toluene.
  • methylaluminoxane (MAO) is used as co-catalyst, for example, toluene may serve as solvent to make it possible to meter the MAO to the polymerisation reactor in solution.
  • Aliphatic polyunsaturated compounds generally contain from 3 to 20 carbon atoms, the double bonds being conjugated or, preferably, unconjugated.
  • Examples hereof are: 1,3-butadiene, isoprene, 2,3-dimethyl-l,3-butadiene, 2-ethyl-l,3- butadiene, piperylene, mycrene, allene, 1,2-butadiene, 1,4,9-decatrienes, 1,4-hexadiene, 1 ,5-hexadiene and 4- methyl-1,4-hexadiene.
  • Alicyclic polyunsaturated compounds which may or may not contain a bridgeing group, may be either monocyclic or polycyclic.
  • Examples of such compounds are norbornadiene and its alkyl derivatives; the alkylidene norbornenes, in particular the 5-alkylidene-2-norbornenes, in which the alkylidene group contains from 1 to 20, preferably from 1 to 8 carbon atoms; the alkenyl norbornenes, in particular the 5-alkenyl-2-norbornenes, the alkenyl group of which contains from 2 to 20, preferably from 2 to 10 carbon atoms, for example vinylnorbornene, 5-(2 '-methyl-2 'butenyl)-2-norbornene and 5-(3 '-methyl-2 'butenyl)-2-norbornene; dicyclopentadiene and the polyunsaturated compounds of bicyclo-(2,2,1)- heptane, bicyclo-(2,2,2)-octane, bicycl
  • compounds such as 4,7,8,9- tetrahydroindene and isopropylidenetetrahydroindene may be employed.
  • Dicyclopentadiene, 5-methylene-2-norbornene or 5-ethylidene-2-norbornene or 1,4-hexadiene are used in particular. Mixtures of the aforementioned compounds may also be used.
  • the diene may be present in the copolymer in amounts of up to 30 % (wt), preferably up to 10-15 % (wt).
  • an unsaturated compound containing one or more functional groups such as halogen atoms, OH, OR, COOH, COOR or NH 2 groups may be incorporated in the copolymer if desired, in an amount of up to 20 % (wt).
  • the molar ratio of the monomers applied is dependent on the desired polymer composition. Given the widely varying polymerisation rates of the monomers, it is not possible to give a universal range for the molar ratios.
  • a molar ratio of between 1 : 1 and 1 : 5 will be selected. If a polyunsaturated compound is to be copolymerised, the molar ratio thereof relative to ethylene will usually be from 0.0001 : 1 to 1 : 1.
  • the polymerisation reaction is usually effected at a temperature of between -40 and 200°C, preferably between 10 and 80°C.
  • the pressure will usually be 0.1 - 5 Mpa but higher or lower operating pressures are also possible.
  • the process is preferably conducted continuously but may also be conducted semi-continuously or batchwise.
  • the residence time may vary from a few seconds to a few hours.
  • the residence time will normally be chosen to be between a few minutes and one hour.
  • The-polymerisation may take place in a liquid which is inert with respect to the catalyst, e.g.
  • the operating temperature and pressure may be so chosen that one or more of the applied monomers, particularly the ⁇ -olefin, e.g. propylene, is liquid and is present in so large an amount that it acts as a dispersant. In that case, another dispersant is not needed.
  • the process according to the invention may be conducted in a gas-filled or a liquid- filled polymerisation reactor or in a completely liquid- filled reactor.
  • the use of a heterogenized catalyst allows the polymerisation process to be effected in suspension or in the gas phase.
  • the molecular weight can be adjusted by techniques known to one skilled in the art. More particularly, this can be done by applying chain terminating agents such as diethyl zinc and preferably with hydrogen. Even very small amounts of hydrogen will suitably influence the molecular weight.
  • the polymer may be worked up in various ways. For liquid-phase processes, this may be done by evaporating the solvent or by steam coagulation.
  • Amorphous copolymers obtained by the process according to the invention generally contain between 25 and 85 % (wt) ethylene. However, products with an ethylene content of between 40 and 75 % (wt) are preferred.
  • Such copolymers are suitable for a plurality of applications, e.g. the manufacture of hoses, conveyor belts, sealing profiles. If desired, they may be vulcanized by the usual methods (for instance with the aid of free-radical donors, such as peroxides, or with sulphur) . In order to allow the product to be processed as a rubber, the copolymer may be extended with oil; this is preferably done during the polymerisation process. It is known to add agents so as to prepare a friable bale. This may be effected by, for instance, adding talc or by employing a system as described in EP-A- 427,339. The composition described therein, comprising an inorganic partioning agent, a thickener and binder reagent and an anionic dispersant, has been found to be well suited for use in the products according to the invention.
  • the metallocenes of the present invention exhibit great differences from the traditional V-based Ziegler catalysts (such as V0C1 3 and its derivatives).
  • the metallocene compound has a relatively high affinity to propylene and a much lower affinity to the third monomer.
  • propylene inversion takes place to a much lesser degree (approx. 20% in the case of the traditional catalyst and only approx. 0-5% if a metallocene according to the invention is used, measured with the aid of C13-NMR). Consequently, altogether different EP(D)M structures are obtained.
  • the 2-indenyl compounds are applied in known manner, whether or not in combination with a cocatalyst, which is usually an organometal compound, in which the metal is chosen from group 1, 2, 12 or 13 of the Periodic System of Elements. Preference is given to an aluminium compound.
  • a cocatalyst which is usually an organometal compound, in which the metal is chosen from group 1, 2, 12 or 13 of the Periodic System of Elements.
  • Preference is given to an aluminium compound.
  • aluminium compounds-based cocatalysts reference can be given to for instance EP-A-287,666, pages 20-21.
  • cocatalysts are benzene-insoluble organo-aluminium-oxy compounds as disclosed in EP-A- 360,492. See also US-A-4,769,428 (5th column), where organoaluminium alkyls and linear and cyclic aluminoxanes are used as cocatalysts.
  • the aluminoxanes may be prepared in the manner disclosed in these patent publications; they are also commercially available. Examples of commercially available aluminoxanes include methylaluminoxanes as manufactured by Schering, Ethyl and Akzo.
  • the 2-indenyl compounds according to the invention may also be employed in the polymerisation of olefins without aluminoxanes being used as cocatalysts.
  • the 2-indenyl compounds may, for instance, be converted to cationic compounds, which have catalytic activity. For the conversion into cationic compounds refer to, for instance, WO-A-91,09,882, EP-A-277,004 or WO-A-91,02,012.
  • the 2-indenyl compounds according to the invention in solid form or when suspended in an inert solvent, are highly stable and can therefore be stored for prolonged periods of time.
  • the invention further relates to a polyolefin obtainable by polymerisation of (an) olefin(s) using a 2- indenyl compound according to the invention as a catalyst component.
  • the invention will be illustrated by the following examples and comparative experiments.
  • the indenyl compounds that were synthesized were analyzed through neutron activation analysis and H-NMR (hydrogen nuclear magnetic resonance). Neutron activation analysis was used to determine, for instance, the transition metal and halogen contents.
  • H-NMR resulted in informations about the structure of the indenyl compounds.
  • the H-NMR analyses were conducted using a Bruker AC200 NMR instrument at a frequency of 200 MHz.
  • the samples for NMR analysis were prepared by adding c. 1 ml of deuterobenzene to 1-10 mg of the indenyl compound.
  • the crystallization behaviour of the polymers obtained was determined by differential scanning calorimetry (DSC). After rapidly heating the sample to 200°C and holding it at that temperature for 5 minutes, the sample is cooled to -70°C at the rate of 10°C/minute. The accompanying thermal effects are recorded.
  • a "Hoekstra" value (a measure of the plasticity of the product) was measured on the rubbery polymers. This is done by placing a rubber sheet between two platens at a temperature of 106°C. The platens are positioned at a distance of 1 mm. A load of 10 kg/cm 2 is applied after 30 seconds so as to measure the distance between the platens after 15 seconds. The percentage decrease in thickness is the value of the Hoekstra plasticity.
  • the intrinsic viscosity of the polymers obtained was determined by dissolving in decalin at 130°C.
  • Examples I-III and comparative experiments A-C describe the synthesis of unbridged indenyl compounds.
  • Examples IV-IX and comparative experiments D-G concern the application of these unbridged indenyl compounds as catalysts for the polymerisation of (an) olefin(s).
  • Examples X-XIV describe the synthesis of bridged 2-indenyl compounds whilst examples XV-XIX concern the polymerisation of (an) olefin(s) with these compounds.
  • Examples XX-XXIII describe the synthesis of unbridged 2-indenyl compounds having a hetero atom containing group as substituent on the 2-position of the indenyl, whilst examples XXIV-XXVII describe the polymerisation of an olefin with these compounds.
  • n-butyllithium (n-BuLi) (1.6 M solution in hexane) was added to a solution of 3.72 grams of 2-methylindene in 40 ml of diethylether at - 56°C. On removal of the coolant the reaction mixture was stirred for 2 hours (room temperature was reached after 30 minutes). The reaction mixture was then cooled to - 56°C and combined with a suspension of 3.33 grams of zirconium tetrachloride in 40 ml of diethylether (also previously cooled to - 56°C). The coolant was removed and the reaction mixture was stirred for 2 hours (reaction toke place within a few seconds).
  • n-BuLi n-butyllithium
  • Example 1.2 As in Example 1.2, but this time with: 3.98 grams of 1-methylindene, 18.3 ml of n-BuLi, 3.59 grams of zirconium tetrachloride.
  • reaction product of Example I was used for solution copolymerisation of ethylene and propylene.
  • Reaction product 1 in spirit (slurry) and MMAO® (Akzo, modified MAO 3A) in heptane were added to a 1.5-litre reactor filled with 45.0 ml of gasoline, at a feed temperature of 30 °C and a pressure of 0,7 MPa.
  • An after- rinse was performed with 50 ml of gasoline.
  • the propylene/ethylene ratio in the gas phase was 2.
  • the zirconium concentration in the reactor was 4 ⁇ mol/1, the Al/Zr ratio was 1000.
  • Example II The reaction product of Example I was used for solution polymerisation of ethylene and propylene as described in Example VI. This time the Al/Zr ratio was 2500. After 30 minutes' polymerisation, during which the maximum polymerisation temperature was 41 °C, 16 grams of clear rubber (Hoekstra: 45) without visible homopolymer by-product was isolated and worked up. The C 3 content was 52 wt.% and the DSC measurement revealed no crystallization peak above -50 °C.
  • Example II Ethylene/propylene polymerisation
  • the reaction product of Example II was used for solution copolymerisation of ethylene and propylene as described in Example VI.
  • the Al/Zr ratio was 2500.
  • 10 grams of clear rubber (Hoekstra: 72) without visible homopolymer by ⁇ product was drained and worked up.
  • the C 3 content was 51 wt.%; the DSC measurement revealed no crystallization peak above -50 °C.
  • Example II The reaction product of Example II was used for solution polymerisation of ethylene and propylene as described in Example VI.
  • the Al/Zr ratio was now 1000.
  • the C 3 content was 53 wt.%; the DSC measurement revealed no crystallization peak above -50 °C.
  • Comparative Experiment F Ethylene/propylene polymerisation Polymerisation as described in Example VI, but this time with the catalyst of Comparative Experiment A and with an Al/Zr ratio of 2500.
  • the product yield was about 20 grams, but the stirrer and the walls were greatly fouled with deposits (mainly polyethylene).
  • Example 1.2 As in Example 1.2, this time with: 1.21 grams of thio(bis(l-benzyl-2-indene) ) , 3.4 ml of n-BuLi, 0.64 gram of zirconium tetrachloride.
  • a solution of 31.3 grams of triethyl- phosphonoacetate in 75 ml of THF was dosed to a suspension of 3.30 grams of sodium hydride in 200 ml of THF, at 15 °C, in five quarters of an hour. Afterwards, the mixture was stirred at room temperature for another 30 minutes. While the mixture was being cooled with a water bath, a solution of 18.1 grams of 2-indanone in 75 ml of THF was dosed to it in 1 hour, followed by stirring for three quarters of an hour at room temperature.
  • Example XI Ethylene was polymerised under conditions as described in Example IV. This time, however, the catalyst of Example XI was used, in the form of 1 ml of a 0.015 M suspension in gasoline. This catalyst was premixed with 10 ml of a 1.6 M MAO/toluene solution (Schering) for 1 minute before the mixture was added to the reactor at a reactor temperature of 155 °C. The polymerisation was stopped after 7 minutes. Yield: 42.5 grams of polyethylene.
  • Example XVII Ethylene polymerisation Polymerisation as described in Example XV, but this time with using 1 ml of a 0.015 M suspension of the catalyst of Example XIV and 10 ml of a 1.6 M MAO/toluene solution (Schering). Yield: 29 grams of polyethylene. Comparative Experiment H Ethylene polymerisation
  • Example XI The reaction product of example XI was used for the solution copolymerisation of ethylene and propylene as described in Example VI.
  • the Zr concentration in the reactor was 8 ⁇ mol/1; the feed temperature was 40 °C. This time the Al/Zr ratio was 1250.
  • the C 3 content was 53 wt.%; the intrinsic viscosity was 0.1 dl/g.
  • Ethylene/propylene polymerisation The reaction product of example XII was used for the solution copolymerisation of ethylene and propylene as described in Example VI. This time 6 ⁇ mol Zr/1 was used and the Al/Zr ratio was 1670. The propylene/ethylene ratio in the gas phase was 6; the feed temperature 40 °C. After 30 minutes' polymerisation, during which a maximum reaction temperature of 46 °C occurred, 26 grams of clear rubber without visible homopolymer by-product was isolated and worked up. The C 3 content of the product thus obtained was 62 wt.%; the intrinsic viscosity was 0.1 dl/g.
  • Me 2 Si(3-Me-Cp) 2 ZrCl 2 was used for the solution copolymerisation of ethylene and propylene as described in Example VI.
  • the Al/Zr ratio was 2500. After 30 minutes' polymerisation, 5.2 grams of low-molecular-weight inhomogeneous product was isolated and worked up.
  • V0C1 3 was used as catalyst, in a concentration of 12.5 ⁇ mol/1.
  • sesquiethyl aluminium chloride was used, in such an amount that the Al/V ratio was 16.
  • DCPAE dichlorophenyl- acetic acid ethyl ester
  • a solution polymerisation of ethylene and propylene was carried out as described in Example VI.
  • the propylene/ethylene ratio in the gas phase was 2 and the inlet temperature was 30 °C. After 10 minutes' polymerisation, during which a maximum reaction temperature of 40 °C occurred, the catalyst no longer showed any activity; 9 grams of clear rubber was obtained (Hoekstra 85).
  • the C 3 content of this rubber was 38 wt.%; the DSC measurement revealed a crystallization temperature of -6 °C.
  • Example 1.2 As in Example 1.2, this time with: 1.74 grams of methyl(2-indenyl)sulphide, 7.0 ml of n-BuLi solution,
  • Example XX.2 As in Example XX.2, this time with: 1.46 grams of benzyl(2-indenyl)sulphide, 3.8 ml n-BuLi solution, 0.72 grams of zirconiumtetrachloride.
  • To the reactor was added 3.3 ml of MAO (1.6 M in toluene).
  • 25 ml of gasoline and 0.25 ml of a 0.01 M solution of a 2-indenyl compound were mixed and added to the reactor.
  • An after-rinse was performed with 25 ml of gasoline.
  • After 7 minutes of polymerisation at 50 °C and 0.7 MPa the polymerisation was stopped by releasing the pressure to atmospheric pressure and the polyethylene was isolated and dried.
  • the respective 2-indenyl compounds used are the compounds of Examples XX to XXIII.
  • the polymerisation results are given in the following table:

Abstract

The invention relates to an indenyl compound of the general formula: R'Ind-M-(Cp)Qk in which the symbols have the following meanings: Ind: an indenyl group, R': a substituent, other than hydrogen, to the Ind group, Cp: a cyclopendadienyl group, M: a transition metal from group 3, 4, 5 or 6 of the Periodic System of Elements, Q: a ligand to M and k is an integer linked to the valence of M. The invention is characterized in that the R' group is bound to the Ind group at the 2-position. The indenyl compound is a catalyst component for the polymerization of olefins. The invention also relates to polymers obtainable with such indenyl compounds.

Description

INDENYL COMPOUNDS AND CATALYST COMPONENTS FOR THE POLYMERISATION OF OLEFINS i
The invention relates to indenyl compounds that 10 can be used as catalyst component for the polymerisation of olefins. The invention also relates to a process for the polymerisation of olefins and to a polyolefin.
Indenyl compounds are known as catalyst component for olefin polymerisation. The catalysts 15 obtained using indenyl compounds exhibit a high polymerisation activity. See for example DE-A-3,840,772. The known indenyl compounds have the general formula:
R'Ind-M-(Cp)Ok (1)
20 in which the symbols have the following meanings:
Ind an indenyl group,
R' a substituent, other than hydrogen, to the Ind group, 25 Cp a cyclopentadienyl group,
M a transition metal from group 3, 4, 5 or 6 of the Periodic System of Elements, 0 a ligand to M.
30 The Periodic System of Elements is understood to be the new IUPAC version as printed on the inside cover of the Handbook of Chemistry and Physics, 70th edition, CRC Press, 1989-1990.
In formula (1), k is an integer linked to the
35 valence of M in the following manner: k equals the valence of M minus two divided by the valence of the 0 group. The Ind group and the Cp group are both bound to the metal M. The said compounds are regarded as belonging to the metallocene compounds (metallocenes).
One of the aims of the invention is to provide new indenyl compounds with the general formula (1). Another aim is to provide an indenyl compound having favourable properties as a catalyst component in olefin polymerisation.
The invention concerns an indenyl compound having the general formula (1), characterized in that the substituent R' in formula (1) is bound to the Ind group at the 2-position. Here and hereinafter such a compound will be referred to as 2-indenyl compound (2-Ind). In the known indenyl compounds the substituent R' is bound to the Im¬ position of the indenyl ring; the known indenyl compounds are therefore 1-indenyl compounds.
In general and in this description, the substituent locants of the indenyl ring are numbered in accordance with the IUPAC Nomenclature of Organic Chemistry, 1979, rule A 21.1. The numbering of the substituent locants for indene is given below. This numbering is analogous in the case of an indenyl ring:
Indene
Figure imgf000004_0001
According to the invention 2-indenyl compounds were found to exhibit an activity different from that of the known 1-indenyl compounds in olefin polymerisation. In the solution polymerisation of olefins, in particular in the polymerisation to polyethylene, such compounds exhibit higher activity. In the production of ethylene-α-alkene- (third monomer) rubbers (the so-called EA(D)M rubbers) they lead to products that differ from the usual products obtained with metallocenes, among other things to products with a very low content of crystalline material. In the compounds according to the invention the Cp group in formula (1) is a cyclopentadienyl group or a derivative thereof, like for example a fluorenyl group or an indenyl group, all of them whether or not substituted. From EP-A-485,821 and EP-A-485,823 bisindenyl- metallocenes are known having a bridge coupled to the Im¬ positions of the indenylgroups. Such metallocenes are expressly excluded.
In EP-A-500,944 an halogenated metallocene, bis(2,3-dimethyl-l-indenyl)zirconiumdichloride is mentioned. This metallocene is also expressly excluded from the 2-indenyl compounds of the invention.
EP-A-372,414 indicates two specific halogenated, bridged metallocenes. The chemical names of the two metallocenes (of formula II-l and II-2 on page 5 of said EP-A) are: ethylene-1-(3-but-3-enyl)inden-1-yl)-2-( (1-but- 3-enyl)-inden-2-yl)zirconiumdichloride, and ethylene-l-( (3-allyldimethylsilyl)-inden-l-yl)- 2-( (1-allyldimethylsilyl)-inden-2-yl)zirconium- dichloride. Also these two bisindenyl compounds are expressly excluded from the 2-indenyls of the invention.
The above mentioned disclaimers relative to the prior art are justified as neither in the texts nor in examples thereof it is disclosed or suggested that these metallocenes, in which the above indicated Cp-group is an indenylgroup, form part of the generic group of 2-indenyl- metallocenes, having the properties as described before. Besides being present in the indenyl compound at the 2-position of the R' group, the indenyl group (the Ind group in formula (1)) may optionally also be substituted at other positions. The Cp group may also be substituted. As R' group, a hydrocarbon group (like alkyl, aralkyl, aryl) or a group with at least one heteroatom from group 14, 15 or 16 of the Periodic System of Elements may be used. Examples of such a heteroatom containing group are: alkylsulphides (like MeS-, PhS-, n-butyl-S-), amines (like Me2N-, n-butyl-N-), Si or B containing groups (like Me3Si- or Et2B-) or P-containing groups (like Me2P- or Ph2P-). Hydrogenated forms of 2-indenyl compounds also fall within the spirit of the invention.
As a substituent at a position other than the 2- position of the Ind group or the Cp group such groups as indicated above for R' may also be used.
According to the invention, when R' is a hydrocarbon group, R ' is preferably an alkyl group, more in particular an alkyl group with 1-4 carbon atoms.
The 0 group in the compounds according to the invention comprises one or more uni- or polyvalent anionic ligands to the transition metal. As examples of such ligands, which may be the same or different, the following can be mentioned: a hydrogen atom, a halogen atom, an alkyl group, an aryl group, an aralkyl group, an alkoxy group, an aryloxy group, a group with a heteroatom chosen from group 14, 15 or 16 of the Periodic System of Elements, such as
- an amine group or amide group,
- an S compound, such as sulphide, sulphite, sulphate, thiol, sulphinate,
- a P compound, such as phosphine, phosphite, phosphate. The skilled .in the art can determine the suitability of these and other ligands through simple experimenting. The number of 0 groups in the 2-indenyl compound according to the invention (index k in formula (1)) is determined by the valence of the transition metal M and the valence of the Q groups itself.
The transition metal in the 2-indenyl compound (the M group) is chosen from groups 3 through 6 of the Periodic System of Elements. The transition metal is preferably chosen from the group Ti, Zr, Hf, V, Nb, Cr, Ta, Sm and Mo. Zr, Hf or Ti are greatly preferred.
Another preferred embodiment of the invention is formed by compounds in which the Cp group is a 2-indenyl group with the formula:
R"Ind (3)
where R" is a substituent other than hydrogen at the 2- position of the Ind group. As R" group, a hydrocarbon group (like alkyl, aryl, aralkyl) or a group with at least one heteroatom from group 14, 15 or 16 of the Periodic System of Elements may be used. Such a substituent can be the same as or different from the substituent used as R'. The R" group, when being a hydrocarbon group, is preferably an alkyl group, in particular an alkyl group with 1-4 carbon atoms. When used as, for example, catalyst in the solution polymerisation of ethylene at reaction temperatures of at least 130°C these compounds have a high catalytic activity, and in the production of ethylene-α- alkene-(third monomer) rubbers they lead to products with a very low content of crystalline material.
In another preferred embodiment of the invention, the indenyl group of formula (1) is a group in which is R' is linked to the Cp group in formula (1). These compounds, in which Rl forms a bridge between the 2- position of the Ind group and the Cp group in formula (1), are referred to as bridged 2-indenyl compounds according to the invention. The other compounds according to formula (1), without the bridge between the 2-indenyl group and the Cp group, are referred to as unbridged 2-indenyl compounds. In particular, in a bridged 2-indenyl compound the Cp group in formula (1) is a 2-indenyl group as well, which is bound to the R' group at the 2-position. Such compounds according to the invention are referred to as bridged bis(2-indenyl) compounds; in such a case the ' group forms a bridge between two 2-indenyl groups, hence the term bridged bis(2-indenyl) compound. The formula of these bridged bis(2-indenyl) compounds according to the invention may be represented as follows:
Figure imgf000008_0001
where
R is a group derived from R'. In a bridged bis(2-indenyl) compound according to the invention, R can be chosen to be a hydrocarbon group (like an alkenyl group, an arylalkenyl group) or a group with at least one heteroatom from group 14, 15 or 16 of the Periodic System of Elements. Preferably the choice of the R group, when being a hydrocarbon group, is between a methylydene group and an ethylydene group. If R contains a heteroatom, this heteroatom is preferably chosen from the group comprising silicon, nitrogen, phosphorus, oxygen or sulphur. Examples from R-groups containing a heteroatom are: sulphur or -(CH2)2-S-(CH2)2-, oxygen, Me2Si=,
-SiMe2-SiMe2-, GeMe2-, PhP= or PhN=. The hydrocarbon groups in these R-groups containing a heteroatom may be varied and can be an alkyl, aryl or aralkylgroup. With such bridged bis(2-indenyl) compounds as catalyst component, good results are obtained in the solution polymerisation of ethylene and in the synthesis of EA(D)M rubbers. The 2-indenyl compounds according to the invention can be prepared via different synthesis routes, consisting of synthesis steps known as such. They can for example be prepared by converting a 2-indene compound into its anion. Compounds that are suitable for converting the 2-indene compound into the anion are organometallic compounds, amines, metal hydrides and alkaline or alkaline earth metals. Organolithium, organomagnesium and organosodium compounds can for example be used for this purpose, but also sodium or calcium. In particular organolithium compounds are highly suitable, preferably methyl-lithium or n-butyl-lithium.
The elucidation of the further synthesis steps will be based on the use of a lithium anion, but the invention is by no means limited to this. In the case of non-bridged ligands the conversion takes place via reaction with 1 equivalent organolithium compound to obtain the mono-anion, and in the case of bridged ligands via reaction with 2 equivalents organolithium compound to obtain the di-anion. The 2-indenyl anion thus prepared is subsequently converted into the 2-indenyl compound of the invention by trans-metalation with a compound of a transition metal from groups 3, 4, 5 or 6 of the Periodic System of Elements (M in formula (1)). See for example EP-A-420,436, EP-A-427,697. The process described in NL-A-91,011,502 is particularly suitable. Examples of transition metal compounds that are suitable for trans- metalation are TiCl4, ZrCl4, HfCl4, Zr(OBu)4 and Zr(OBu)2Cl2. The trans-metalation is preferably carried out as in NL-A-91,011,502, in a solvent or in a combination of solvents that weakly coordinate to transition metals from the groups 3, 4, 5 or 6 with at most 1 mole equivalent, relative to the transition metal compound started from, of a Lewis base of which the conjugated acid has a pKa greater than -2.5. Examples of suitable solvents/dispersants (pKa of conjugated acid ≤ -2.5) are ethoxyethane, dimethoxyethane, isopropoxyisopropane, n- propoxy-n-propane, methoxybenzene, methoxymethane, n- butoxy-n-butane, ethoxy-n-butane and dioxane. Part of the reaction medium may consist of hydrocarbons (hexane and the like). In the said trans-metalation LiCl is formed besides the metallocene. This usually precipitates in the dispersants used. If the metallocene precipitates too, the combination of metallocene and LiCl as such can be used with a co-catalyst (aluminium compound or cation- generating agent) for the polymerisation of olefins. The LiCl may also be separated from the metallocene, for example by dissolving the metallocene in dichloromethane and filtering LiCl off. If the metallocene dissolves in the solvent used in the synthesis, the LiCl can be separated at once by filtration. The 2-indene compounds mentioned heretofore as compounds started from can be formed from commercially available compounds, via synthess routes consisting of several reaction steps known per se. The synthesis route is chosen on the basis of the 2-indenyl compound desired. The unbridged 2-indenyl compounds, for example, can be prepared from 2-indanones, which are commercially available, via reaction with an alkyl magnesium halide-, followed by dehydration. The synthesis of the bridged 2- indenyl compounds strongly depends on the 2-indenyl compound desired. Various synthesis routes are described in the examples given hereafter.
The 2-indenyl compounds according to the invention can be used, via methods known for metallocenes, as catalyst component for the polymerisation of one or more olefins. Particularly the olefin(s) is/are chosen from the group comprising α-olefins, internal olefins and diolefins. Mixtures of these can also be used.
The invention relates in particular to a process for the polymerisation of (an) α-olefin(s). The α-olefin(s) is/are preferably chosen from the group comprising ethylene, propylene, butene, pentene, heptene and octene, while mixtures can also be used. More preferably, ethylene and/or propylene is/are used as α-olefin. The use of such olefins leads to the formation of crystalline polyethylene homopolymers and copolymers of both low and high density (HDPE, LDPE, LLDPE, etc.), and polypropylene homopolymers and copolymers (PP and EMPP). The monomers needed fur such products and the processes to be used are known to the skilled in the art. The process according to the invention is also eminently suitable for the preparation of amorphous or rubbery copolymers based on ethylene and another α-olefin. Propylene is preferably used as the other α-olefin, so that EPM rubber is formed. It is also quite possible to use a diene besides ethylene and the other α-olefin, so that a so-called EADM rubber is formed, in particular EPDM (ethylene propylene diene rubber).
The 2-indenyl compounds according to the invention can be used as catalyst, both supported and unsupported. The supported catalysts are mainly used in gas-phase and slurry processes. The support is any support known as support for metallocene catalysts, for example Si02 or A1203.
The 2-indenyl compounds according to the invention are particularly suitable for use as unsupported catalyst in solution polymerisation processes. In solution polymerisation the known solvents may be used. Preferably aliphatic hydrocarbons, such as hexane and heptane, and mixtures of aliphatic hydrocarbons are used.
If an aliphatic hydrocarbon is used as solvent, the solvent may still contain small amounts of aromatic hydrocarbon, for example toluene. If methylaluminoxane (MAO) is used as co-catalyst, for example, toluene may serve as solvent to make it possible to meter the MAO to the polymerisation reactor in solution.
In the solution polymerisation of ethylene or of ethylene with other α-olefins and/or non-conjugated dienes at comonomer contents of up to 25% reactor temperatures of at least 130 °C are used, in order to keep the polymer produced in solution. At weight percentages of incorporated comonomer of from 30 to 80% the catalysts according to the invention yield such homogeneous products that the polymerisation can be carried out at much lower reactor temperatures ( ≥ 30 °C) without the polymer formed precipitating from the solution. Suitable other α-olefins are for example propylene, butene, hexene and octene. Polymerisation of the olefin can take place in a known manner, in the gas phase as well as in a liquid reaction medium. In the latter case both solution polymerisation and suspension polymerisation are options.
The process according to the invention will hereafter be elucidated with reference to the EP(D)M preparation known per se, which is representative of the olefin polymerisations meant here. For the preparation of other polymers based on an olefin the reader is emphatically referred to the multitude of publi cions on this subject.
As suitable α-olefins that may be uf-ja as monomer besides ethylene in the preparation of an EA(D)M polymer, the following may be mentioned: propylene, butene-1, pentene-1, hexene-1, octene-1 or the bran neα isomers thereof, for example 4-methylpentene-l, and ix. addition styrene, α-methylstyrene. Mixtures of these alkenes may also be used, propylene and/or butene-1 being preferred.
As diene to be used in such an amorphous copolymer a polyunsaturated compound is started from, which may be used and serves to incorporate unsaturation in the polymer; it contains at least two C=C bonds and may be aliphatic or alicyclic. Aliphatic polyunsaturated compounds generally contain from 3 to 20 carbon atoms, the double bonds being conjugated or, preferably, unconjugated. Examples hereof are: 1,3-butadiene, isoprene, 2,3-dimethyl-l,3-butadiene, 2-ethyl-l,3- butadiene, piperylene, mycrene, allene, 1,2-butadiene, 1,4,9-decatrienes, 1,4-hexadiene, 1 ,5-hexadiene and 4- methyl-1,4-hexadiene.
Alicyclic polyunsaturated compounds, which may or may not contain a bridgeing group, may be either monocyclic or polycyclic. Examples of such compounds are norbornadiene and its alkyl derivatives; the alkylidene norbornenes, in particular the 5-alkylidene-2-norbornenes, in which the alkylidene group contains from 1 to 20, preferably from 1 to 8 carbon atoms; the alkenyl norbornenes, in particular the 5-alkenyl-2-norbornenes, the alkenyl group of which contains from 2 to 20, preferably from 2 to 10 carbon atoms, for example vinylnorbornene, 5-(2 '-methyl-2 'butenyl)-2-norbornene and 5-(3 '-methyl-2 'butenyl)-2-norbornene; dicyclopentadiene and the polyunsaturated compounds of bicyclo-(2,2,1)- heptane, bicyclo-(2,2,2)-octane, bicyclo-(3,2,1)-octane and bicyclo-(3,2,2)-nonane, at least one of the rings being unsaturated. Furthermore, compounds such as 4,7,8,9- tetrahydroindene and isopropylidenetetrahydroindene may be employed. Dicyclopentadiene, 5-methylene-2-norbornene or 5-ethylidene-2-norbornene or 1,4-hexadiene are used in particular. Mixtures of the aforementioned compounds may also be used.
The diene may be present in the copolymer in amounts of up to 30 % (wt), preferably up to 10-15 % (wt). In addition to or in place of the diene, an unsaturated compound containing one or more functional groups such as halogen atoms, OH, OR, COOH, COOR or NH2 groups may be incorporated in the copolymer if desired, in an amount of up to 20 % (wt). The molar ratio of the monomers applied is dependent on the desired polymer composition. Given the widely varying polymerisation rates of the monomers, it is not possible to give a universal range for the molar ratios. Normally, for the copolymerisation of ethylene and propylene a molar ratio of between 1 : 1 and 1 : 5 will be selected. If a polyunsaturated compound is to be copolymerised, the molar ratio thereof relative to ethylene will usually be from 0.0001 : 1 to 1 : 1.
The polymerisation reaction is usually effected at a temperature of between -40 and 200°C, preferably between 10 and 80°C. The pressure will usually be 0.1 - 5 Mpa but higher or lower operating pressures are also possible. The process is preferably conducted continuously but may also be conducted semi-continuously or batchwise. The residence time may vary from a few seconds to a few hours. The residence time will normally be chosen to be between a few minutes and one hour. The-polymerisation may take place in a liquid which is inert with respect to the catalyst, e.g. in one or more saturated aliphatic hydrocarbons such as butane, pentane, hexane, heptane, pentamethylheptane or petroleum fractions; in aromatic hydrocarbons, e.g. benzene or toluene, or in halogenated aliphatic or aromatic hydrocarbons, e.g. tetrachloroethylene. The operating temperature and pressure may be so chosen that one or more of the applied monomers, particularly the α-olefin, e.g. propylene, is liquid and is present in so large an amount that it acts as a dispersant. In that case, another dispersant is not needed. The process according to the invention may be conducted in a gas-filled or a liquid- filled polymerisation reactor or in a completely liquid- filled reactor. The use of a heterogenized catalyst allows the polymerisation process to be effected in suspension or in the gas phase.
The molecular weight can be adjusted by techniques known to one skilled in the art. More particularly, this can be done by applying chain terminating agents such as diethyl zinc and preferably with hydrogen. Even very small amounts of hydrogen will suitably influence the molecular weight.
After polymerisation, the polymer may be worked up in various ways. For liquid-phase processes, this may be done by evaporating the solvent or by steam coagulation.
Amorphous copolymers obtained by the process according to the invention generally contain between 25 and 85 % (wt) ethylene. However, products with an ethylene content of between 40 and 75 % (wt) are preferred.
Such copolymers are suitable for a plurality of applications, e.g. the manufacture of hoses, conveyor belts, sealing profiles. If desired, they may be vulcanized by the usual methods (for instance with the aid of free-radical donors, such as peroxides, or with sulphur) . In order to allow the product to be processed as a rubber, the copolymer may be extended with oil; this is preferably done during the polymerisation process. It is known to add agents so as to prepare a friable bale. This may be effected by, for instance, adding talc or by employing a system as described in EP-A- 427,339. The composition described therein, comprising an inorganic partioning agent, a thickener and binder reagent and an anionic dispersant, has been found to be well suited for use in the products according to the invention.
In the preparation of EP(D)M the metallocenes of the present invention exhibit great differences from the traditional V-based Ziegler catalysts (such as V0C13 and its derivatives). For example, the metallocene compound has a relatively high affinity to propylene and a much lower affinity to the third monomer. Also, propylene inversion takes place to a much lesser degree (approx. 20% in the case of the traditional catalyst and only approx. 0-5% if a metallocene according to the invention is used, measured with the aid of C13-NMR). Consequently, altogether different EP(D)M structures are obtained.
The 2-indenyl compounds are applied in known manner, whether or not in combination with a cocatalyst, which is usually an organometal compound, in which the metal is chosen from group 1, 2, 12 or 13 of the Periodic System of Elements. Preference is given to an aluminium compound. For aluminium compounds-based cocatalysts, reference can be given to for instance EP-A-287,666, pages 20-21. Also suitable as cocatalysts are benzene-insoluble organo-aluminium-oxy compounds as disclosed in EP-A- 360,492. See also US-A-4,769,428 (5th column), where organoaluminium alkyls and linear and cyclic aluminoxanes are used as cocatalysts. The aluminoxanes may be prepared in the manner disclosed in these patent publications; they are also commercially available. Examples of commercially available aluminoxanes include methylaluminoxanes as manufactured by Schering, Ethyl and Akzo. The 2-indenyl compounds according to the invention may also be employed in the polymerisation of olefins without aluminoxanes being used as cocatalysts. The 2-indenyl compounds may, for instance, be converted to cationic compounds, which have catalytic activity. For the conversion into cationic compounds refer to, for instance, WO-A-91,09,882, EP-A-277,004 or WO-A-91,02,012.
The 2-indenyl compounds according to the invention, in solid form or when suspended in an inert solvent, are highly stable and can therefore be stored for prolonged periods of time.
The invention further relates to a polyolefin obtainable by polymerisation of (an) olefin(s) using a 2- indenyl compound according to the invention as a catalyst component. This particularly concerns EA(D)M polymers that stand out from state-of-the art products by a very small number of α-olefine inversions; the products according to the invention preferably have 0-5% α-olefine inversions in the chain. The invention will be illustrated by the following examples and comparative experiments. The indenyl compounds that were synthesized were analyzed through neutron activation analysis and H-NMR (hydrogen nuclear magnetic resonance). Neutron activation analysis was used to determine, for instance, the transition metal and halogen contents. H-NMR resulted in informations about the structure of the indenyl compounds. The H-NMR analyses were conducted using a Bruker AC200 NMR instrument at a frequency of 200 MHz. The samples for NMR analysis were prepared by adding c. 1 ml of deuterobenzene to 1-10 mg of the indenyl compound.
The crystallization behaviour of the polymers obtained was determined by differential scanning calorimetry (DSC). After rapidly heating the sample to 200°C and holding it at that temperature for 5 minutes, the sample is cooled to -70°C at the rate of 10°C/minute. The accompanying thermal effects are recorded. A "Hoekstra" value (a measure of the plasticity of the product) was measured on the rubbery polymers. This is done by placing a rubber sheet between two platens at a temperature of 106°C. The platens are positioned at a distance of 1 mm. A load of 10 kg/cm2 is applied after 30 seconds so as to measure the distance between the platens after 15 seconds. The percentage decrease in thickness is the value of the Hoekstra plasticity.
The intrinsic viscosity of the polymers obtained was determined by dissolving in decalin at 130°C.
Examples
Examples I-III and comparative experiments A-C describe the synthesis of unbridged indenyl compounds.
Examples IV-IX and comparative experiments D-G concern the application of these unbridged indenyl compounds as catalysts for the polymerisation of (an) olefin(s).
Examples X-XIV describe the synthesis of bridged 2-indenyl compounds whilst examples XV-XIX concern the polymerisation of (an) olefin(s) with these compounds. Examples XX-XXIII describe the synthesis of unbridged 2-indenyl compounds having a hetero atom containing group as substituent on the 2-position of the indenyl, whilst examples XXIV-XXVII describe the polymerisation of an olefin with these compounds.
Example I
1.1. Synthesis of 2-methylindene 50 ml of diethylether was added to 2.5 grams of magnesium. A solution of 14.3 grams of methyliodide in 50 ml of diethylether was added for 1 hour while cooling with a water bath. The reaction mixture was then stirred at room temperature for 30 minutes. To this reaction mixture was added a solution of 13.2 grams of 2-indanone in 40 ml of diethylether, whereupon the mixture was stirred for 30 minutes. Hereafter, 100 ml of water was added. The organic layer was •separated from the water layer. This water layer was washed twice with 50 ml of dichloromethane, whereafter the combined organic layers were dried on magnesium sulphate. On filtering off the drying agent, the filtrate was evaporated, leaving 14.0 grams of residue. This residue was dissolved in 100 ml of toluene, 4 drops of concentrated sulphuric acid were added and the resulting reaction mixture was refluxed for 30 minutes. After cooling down to room temperature, the mixture was washed once with 50 ml of water. The toluene was evaporated and the residue was vacuum distilled. Yield: 4.0 grams of 2- methylindene (30%).
1.2. Synthesis of bis(2-methylindenyl) zirconium dichloride
17.9 ml of n-butyllithium (n-BuLi) (1.6 M solution in hexane) was added to a solution of 3.72 grams of 2-methylindene in 40 ml of diethylether at - 56°C. On removal of the coolant the reaction mixture was stirred for 2 hours (room temperature was reached after 30 minutes). The reaction mixture was then cooled to - 56°C and combined with a suspension of 3.33 grams of zirconium tetrachloride in 40 ml of diethylether (also previously cooled to - 56°C). The coolant was removed and the reaction mixture was stirred for 2 hours (reaction toke place within a few seconds). Hereafter, the solid (bis(2- methylindenyl) zirconium dichloride with complexed lithium chloride) was filtered off. The residue obtained was washed once with 25 ml of diethylether and twice with 50 ml of gasoline (which is a mixture of aliphatic hydrocarbons with a boiling range from 65 - 70°C) and then vacuum dried for some hours. Yield: 5.27 grams of a yellow solid, bis(2-methylindenyl) zirconium dichloride. Exampl e 2
11.1. Synthesis of 2-ethylindene
The same synthesis route was followed as in example 1.1 except that ethyl magnesium bromide (70 ml 3.0 M in diethylether) and 13.4 grams of 2-indanone in 75 ml diethylether were used. The excess Grignard compound was neutralized with hydrochloric acid. This time the second step was effected with oxalic acid (15.2 grams) and 200 ml of water in two hours and with refluxing for a quarter. After this step the product was extracted with diethylether (3 times 50 ml). After the solvent had been evaporated, purification took place through a silica column (mobile phase 40-60 petroleum ether). Yield: 4.5 grams of 2-ethylindene (31 %).
11.2. Synthesis of bis(2-ethylindenyl)zirconiumdichloride
As in example 1.2 except with: 2.45 grams of 2-ethylindene 10.2 ml of n-BuLi 2.00 grams of zirconium tetrachloride.
Obtained was 2.6 grams of a yellow solid: bis(2- ethylindenyl) zirconium dichloride.
Example III III.l. Synthesis of 2-butylindene
Procedure as in example 1.1 except with: 2.4 grams of magnesium, 14.0 grams of 1-bromobutane, 13.3 grams of 2-indanone, solvent diethylether. Water and hydrochloric acid were added after reaction. The organic layer was separated from the water layer, which was washed three times with diethylether, and the combined organic layers were evaporated, the residue being mixed with toluene (150 ml). The mixture was refluxed with concentrated sulphuric acid (4 drops). After reacting, the mixture was washed with water (two times 50 ml), evaporated and purified through a silica column. Yield: 7.0 grams of 2-butylindene (41 %). III.2. Synthesis of bis(2-butylindenyl) zirconium dichloride
As in example 1.2 except with: 3.74 grams of 2-butylindene 13.6 ml of n-BuLi
2.53 grams of zirconium tetrachloride.
The product was dissolved in diethylether and passed through a glass filter (for removal of lithium chloride). After evaporating the filtrate, 3.31 grams of a solid compound, bis(2-butylindenyl) zirconium dichloride, was obtained.
Comparative experiment A
A.l. Synthesis of 1-methylindene Indene was reacted with BuLi to form indenyl lithium, which compound was reacted with methyl iodide to form 1-methylindene. Use was made of: 18.2 grams of indene, 100 ml of n-BuLi solution, 22.0 grams of methyl iodide. Yield: 13.2 grams of 1-methylindene (65 %).
A.2. Synthesis of bis(1-methyl-indenyl) zirconium dichloride
As in Example 1.2, but this time with: 3.98 grams of 1-methylindene, 18.3 ml of n-BuLi, 3.59 grams of zirconium tetrachloride.
4.20 grams of a solid yellow compound, bis(l- methyl-indenyl) zirconium dichloride, was obtained.
Comparative Experiment B
B.l. Synthesis of 1-ethylindene
As in comparative experiment A.l, but this time with: 17.6 grams of indene,
100 ml of n-BuLi solution, 23.6 grams of ethyl iodide.
Yield: 15.2 grams of 1-ethylindene (70%). B.2. Synthesis of bis(l-ethylindenyl) zirconium dichloride As in Example 1.2, but this time with:
4.04 grams of 1-ethylindene,
17.5 ml of n-BuLi, 3.25 grams of zirconium tetrachloride.
5.20 grams of a solid yellow compound, bis(l- ethyl-indenyl) zirconium dichloride, was obtained.
Comparative Experiment C Cl. Synthesis of 1-butylindene
As comparative experiment A.l, but this time with lithium diisopropylamide prepared in situ. The following ingredients were used:
15 ml of diisopropylamine, 60 ml of BuLi solution,
11.9 grams of indene,
13.8 grams of butylbromide.
Yield: 5.1 grams of 1-butylindene (29%).
C.2. Synthesis of bis(l-butylindenyl) zirconium dichloride As in Example III.2, except with:
2.98 grams of 1-butylindene,
10.8 ml of n-BuLi,
2.02 grams of zirconium tetrachloride. 4.16 grams of a solid yellow compound, bis(l- butyl-indenyl) zirconium dichloride, was obtained.
Example IV
Ethylene polymerisation 425 ml of pentamethylheptane (isododecane, abbreviation PMH) and ethylene were dosed to a 1.3-litre reactor, while the reactor was being heated until a temperature of 140 °C was reached. Next, 25 ml of a methylaluminoxane (MAO) solution in toluene (Schering, 1.6 M) was added. At a temperature of 155 °C 3 ml of a
0.015 M solution of the catalyst of Example III in hexane was added, followed by an after-rinse with 50 ml of PMH. The total system pressure was 2 MPa and was kept constant by adding ethylene. As a result of the reaction (polymerisation), the temperature rose to 200 °C. After 20 minutes the polymerisation was stopped and the polyethylene was isolated and dried. Yield: 72 grams of polyethylene (PE).
Example V
Ethylene polymerisation Polymerisation as in Example IV, except with:
15 ml of an MAO/toluene solution (Schering, 1.6 M) ,
5 ml of a 0.015 M solution of the catalyst of Example III in hexane.
As a result of the reaction (polymerisation), the temperature rose to 191 °C. After 20 minutes the polymerisation was stopped and the polyethylene was isolated and dried. Yield: 111 grams of polyethylene (PE) .
Example VI Ethylene/propylene polymerisation
The reaction product of Example I was used for solution copolymerisation of ethylene and propylene. Reaction product 1 in spirit (slurry) and MMAO® (Akzo, modified MAO 3A) in heptane were added to a 1.5-litre reactor filled with 45.0 ml of gasoline, at a feed temperature of 30 °C and a pressure of 0,7 MPa. An after- rinse was performed with 50 ml of gasoline. The propylene/ethylene ratio in the gas phase was 2. The zirconium concentration in the reactor was 4 μmol/1, the Al/Zr ratio was 1000. After 30 minutes' polymerisation at a maximum polymerisation temperature of 37 °C, 10 grams of clear rubber (Hoekstra: 80), without visible homopolymer by-product, was isolated and worked up. The C3 content was 48 wt.% and the DSC measurement revealed a crystallization peak at -28 °C. Example VII
Ethylene/propylene polymerisation
The reaction product of Example I was used for solution polymerisation of ethylene and propylene as described in Example VI. This time the Al/Zr ratio was 2500. After 30 minutes' polymerisation, during which the maximum polymerisation temperature was 41 °C, 16 grams of clear rubber (Hoekstra: 45) without visible homopolymer by-product was isolated and worked up. The C3 content was 52 wt.% and the DSC measurement revealed no crystallization peak above -50 °C.
Example VIII
Ethylene/propylene polymerisation The reaction product of Example II was used for solution copolymerisation of ethylene and propylene as described in Example VI. The Al/Zr ratio was 2500. After 30 minutes' polymerisation, during which the maximum polymerisation temperature was 38 °C, 10 grams of clear rubber (Hoekstra: 72) without visible homopolymer by¬ product was drained and worked up. The C3 content was 51 wt.%; the DSC measurement revealed no crystallization peak above -50 °C.
Example IX
Ethylene/propylene polymerisation
The reaction product of Example II was used for solution polymerisation of ethylene and propylene as described in Example VI. The Al/Zr ratio was now 1000. After 30 minutes' polymerisation, during which the maximum polymerisation temperature was 36 °C, 8.5 grams of clear rubber (Hoekstra: 78) without visible homopolymer by¬ product was drained and worked up. The C3 content was 53 wt.%; the DSC measurement revealed no crystallization peak above -50 °C.
The products of examples VI-IX had < 2% C3 inversions in the chain. Comparative Experiment D Ethylene polymerisation
Polymerisation took place as described in Example IV, except that the catalyst of Comparative Experiment C was used. The following ingredients were dosed:
2.5 ml of a 0.015 M solution of the catalyst in hexane, 15 ml of MAO (1.6 M, Schering).
Yield: 25 grams of polyethylene.
Comparative Experiment E Ethylene polymerisation
Polymerisation took place as described in Example IV, except that the catalyst of Comparative Eperiment C was used. In addition, MAO and catalyst were premixed for 1 minute and were dosed at an initial temperature of 155 °C. The following ingredients were used:
1 ml of a 0.015 M solution of the catalyst in hexane, 10 ml of MAO (1.6 M, Schering).
Yield: 15 grams of polyethylene.
Comparative Experiment F Ethylene/propylene polymerisation Polymerisation as described in Example VI, but this time with the catalyst of Comparative Experiment A and with an Al/Zr ratio of 2500. The product yield was about 20 grams, but the stirrer and the walls were greatly fouled with deposits (mainly polyethylene).
Comparative Experiment G Ethylene/propylene polymerisation
Polymerisation as described in Example VI, this time with the catalyst of Comparative Experiment B and with an Al/Zr ratio of 2500. The product yield was about 20 grams, but the product was inhomogeneous and the stirrer and the walls were fouled (mainly with polyethylene) . Exampl e X
X.l. Synthesis of indenebromohvdrin
At a temperature of about 4 °C, 7.5 ml of water and 20.3 grams of N-bromosuccinimide were added to 11.6 grams of indene dissolved in 100 ml of dimethylsulphoxide (DMSO). The reaction mixture was stirred for 20 minutes and then poured out into 400 ml of saturated sodium bicarbonate solution. The precipitate was filtered off and washed with 100 ml of water. After recrystallization from a solution in chloroform/hexane the yield was 15.5 grams of indenebromohydrin (73%).
X.2. Synthesis of 2-bromoindene
To 14.3 grams of indenebromohydrin, dissolved in 150 ml of toluene, 0.5 ml of concentrated sulphuric acid was added, followed by stirring for 1 hour with refluxing, the water released being azeotropically separated. After cooling to room temperature, washing with water (two times 50 ml) and evaporation of toluene, the product was vacuum- distilled. Yield: 4.5 grams (43%) of pale yellow/green coloured 2-bromoindene.
X.3. Synthesis of dimethylbis(2-indene)silane
Starting from 4.3 grams of 2-bromoindene, the corresponding Grignard reagent was prepared, which was then added to a solution of 1.2 gram of dichlorodimethylsilane in 40 ml of tetrahydrofuran (THF). The dosing temperature was 45 °C and the dosing time 1 hour. Afterwards, the mixture was stirred for another 3 hours at 45 °C. The product was worked up by successively adding water, evaporating THF, adding diethylether to the residue, washing the organic layer with water, drying this organic layer over magnesium sulphate, evaporating ether and purifying the residue over a silica column (mobile phase: hexane). Yield: 0.43 gram (13.7%) of a viscous, colourless liquid, dimethylbis(2-indene)silane. X. . Synthesis of (dimethylbis(2-indenyl)silane) zirconium dichloride
As in Example 1.2, this time with: 0.71 gram of dimethylbis(2-indene)silane, 3.35 ml of n-BuLi,
0.62 gram of zirconium tetrachloride.
1.15 gram of a solid yellow compound (the compound of the title plus lithium chloride) was obtained.
Example XI
XI.1. Synthesis of thio(bis(2-indene) )
2-Indanone (3.0 g) and Lawesson reagent (see S. Scheibye, R. Shabana and S.-O Lawesson, Tetrahedron 38, (1982), 993) (5.45 g) were heated for 2.5 hours in 40 ml of toluene with refluxing. Next, the reaction mixture was stirred for 12 hours at room temperature, after which the toluene was evaporated. The reaction product was purified with the aid of chromatography. The thio(bis-(2-indene) ) yield was 21 g.
XI.2. Synthesis of (thio(bis(2-indenyl) ) ) zirconium dichloride
As in Example 1.2, this time with: 2.54 grams of thio(bis(2-indene) ) , 12.1 ml of n-BuLi,
2.72 grams of zirconium tetrachloride.
4.54 grams of a solid yellow compound, (thio(bis(2-indenyl) ) ) zirconium dichloride, was obtained.
Example XII
XII.1. Synthesis of thiofbis(l-benzyl-2-indene) )
15.0 grams of sodium carbonate was added to a solution of 13.6 grams of 2-indanone in 100 ml of THF.
Next, a solution of 10.0 grams of pyrrolidine in 40 ml of THF was added to this mixture in 35 minutes, after which the mixture was stirred for 1 hour at room temperature.
Working up of this reaction mixture yielded 18.7 grams (100%) of the corresponding enamine.
Of this enamine, 0.1 mol was refluxed for 7 hours with 19.4 grams of benzylbromide in 150 ml of acetonitrile. After evaporation of the solvent, water (100 ml), acetic acid (25 ml) and 100 ml of dichloromethane were added; the entire mixture was stirred for 18 hours. Working up of the organic layer yielded a product which was purified by vacuum distillation. Yield: 5.2 grams (23%). The so obtained l-benzyl-2-indanone was now reacted with Lawesson's reagent as described in Example XI.1, and after refluxing the mixture was stirred at room temperature for 20 hours. After evaporation of the toluene the product was boiled five times with 200 ml of hexane, after which the hexane layers were combined and the hexane was evaporated. Recrystallization from methanol yielded 2.5 grams (35%) of thio(bis(l-benzyl-2-indene) ) as product.
XII.2. Synthesis of (thio(bis(l-benzyl-2-indenyl) ) ) zirconium dichloride
As in Example 1.2, this time with: 1.21 grams of thio(bis(l-benzyl-2-indene) ) , 3.4 ml of n-BuLi, 0.64 gram of zirconium tetrachloride.
1.11 gram of a solid yellow compound, (thio(bis(l-benzyl-2-indenyl) ) ) zirconium dichloride, was obtained.
Example XIII
XIII.1. Synthesis of ethyl(2-indene)acetate
A solution of 31.3 grams of triethyl- phosphonoacetate in 75 ml of THF was dosed to a suspension of 3.30 grams of sodium hydride in 200 ml of THF, at 15 °C, in five quarters of an hour. Afterwards, the mixture was stirred at room temperature for another 30 minutes. While the mixture was being cooled with a water bath, a solution of 18.1 grams of 2-indanone in 75 ml of THF was dosed to it in 1 hour, followed by stirring for three quarters of an hour at room temperature. Working up was as follows: the reaction mixture was poured out into water, extracted with diethylether, the ether layers were dried over magnesium sulphate, the magnesium sulphate was filtered off, the filtrate evaporated; the yield was 27.4 grams of crude reaction product. After vacuum distillation, 22.4 grams (80%) of the ethyl(2-indene)- acetate was obtained.
XIII.2. Synthesis of 2(2-indene)ethanol
A solution of 7.0 grams of ethyl(2-indene) acetate in 50 ml of diethyl ether was added in drops to a suspension of 1.41 grams of lithium aluminium hydride in 100 ml of diethyl ether, at room temperature. The temperature rose to 30 °C and the total dosing time was 60 minutes. Afterwards, the mixture was stirred for 30 minutes at room temperature. Next, 25 ml of water was added and stirring was continued for 15 minutes. The mixture was poured out into ice, and, after addition of concentrated sulphuric acid, subjected to a standard working-up procedure (vide Example I). The product was purified over a silica column (mobile phase: hexane), the yield being 4.0 grams of pure 2(2-indene)ethanol (72%).
XIII.3. Synthesis of l-bromo-2(2-indene)ethane
To a solution of 7.1 grams of 2(2-indene)ethanol in 100 ml of THF, 11.8 grams of triphenylphosphine and subsequently, in small portions, 8.0 grams of N-bromo- succinimide were added, at room temperature. The total dosing time was 1 hour, which was followed by 30 minutes' stirring at room temperature. The reaction mixture was poured out into 300 ml of hexane and the precipitate formed was filtered off and washed two times with 50 ml of hexane. The combined hexane fractions were evaporated and the product was purified over a silica column (mobile phase: hexane). Yield: 7.9 grams of l-bromo-2(2-indene)- ethane (80%).
XIII.4 Synthesis of l-cyclopentadiene-2(2-indene)ethane To a solution of 120 mmol of cyclopentadiene sodium (NaCp) in 260 ml of THF, a solution of 18.2 grams of l-bromo-2(2-indene)ethane in 100 ml of THF was added in two hours at -35 °C, after which the mixture was stirred for another 30 minutes at this low temperature and subsequently for 16 hours at room temperature. After addition of water, evaporation of THF, extraction with diethyl ether, drying of the organic layers and evaporation of the solvent, the product was purified over silica (mobile phase: petroleumether 40-60). Yield: 7.1 grams (41%) of l-cyclopentadiene-2(2-indene)ethane.
XIII.5 Synthesis of (l-cvclopentadienyl-2(2- indenyl)ethane) zirconium chloride
As in Example 1.2, this time with: 2.94 grams of l-cyclopentadiene-2(2-indene)ethane,
17.6 ml of n-BuLi,
3.2 grams of zirconium tetrachloride.
5.05 grams of solid pale-yellow compound as in the title were obtained. A portion of this product was made free of lithium chloride by extraction with dichloromethane.
Example XIV
XIV.1. Synthesis of 2-hvdroxymethylene-l-indanone To a solution of 15.5 grams of sodium ethoxide in 150 ml of t-butyl-methyl-ether, a solution of 26.7 grams of 1-indanone and 16.2 grams of ethyl formiate in 250 ml of of t-butyl-methyl-ether was added in 1 hour while cooling with a water/ice bath. Afterwards, the reaction mixture was stirred for one-and-a-half hours at room temperature. A solution of 13.7 grams of acetic acid in 100 ml of water was added. After working up of the organic layer, 27.7 grams of product (85%) was obtained. XIV.2. Synthesis of 2-(l-keto-2-indene-methylene)-indan-l- one
After 23.1 grams of 2-hydroxymethylene-l- indanone had been heated to 120 °C for three quarters of an hour, 220 ml of m-xylene were added. After one quarter of an hour the mixture was cooled and the product crystallized. Yield: 11.6 grams (60%).
XIV.3. Synthesis of bis-2-indanone-l-methane An amount of 5 grams of finely ground product obtained in step XIV.2, together with 90 ml of ethylacetate and 1 gram of Raney nickel, was reacted with hydrogen for three-and-a-half hours in an autoclave at 25 °C and 0,54 MPa. The reaction mixture was then filtered off and the filtrate was evaporated to 50%. Addition of hexane and cooling yielded a white crystalline compound. By repeating the crystallization three times, 3.5 grams (70%) of product was ultimately obtained.
XIV.4. Synthesis of bis-2-indenemethane
At 58 °C, 3.99 grams of the diketone of step XIV.3, together with 2 drops of concentrated hydrochloric acid, were added to a solution of 5.95 grams of toluene-4- sulphonhydrazide in 40 ml of 96% ethanol. This reaction mixture was refluxed f.or 10 minutes. After cooling in a water/ice bath, the product (bis-hydrazone) was filtered off, dried and ground (7.68 grams, 87%).
To 10.24 grams of diisopropylamine and 50 ml of tetramethylethylenediamine, 40 ml of 1.6 M MeLi in ether was added for 15 minutes at 0 °C. Five minutes later, 5 grams of the bis-hydrazone was added in 4 minutes, after which the mixture was heated to room temperature. This mixture was stirred for 17 hours. Working up (adding water, working up organic layers) yielded a crude reaction product, which was purified by crystallization from hexane. Yield: 0.47 gram of bis-2-indenemethane. XIV.5. Synthesis of (bis-(2-indenyl)methane) zirconium dichloride
As in Example 1.2, this time with: 0.40 gram bis-(2-indene)methane, 2.0 ml of n-BuLi,
0.40 gram zirconium tetrachloride.
0.56 gram of a solid, orange compound, (bis-(2- indenyl)methane) zirconium dichloride, was obtained.
Example XV
Ethylene polymerisation
Ethylene was polymerised under conditions as described in Example IV. This time, however, the catalyst of Example XI was used, in the form of 1 ml of a 0.015 M suspension in gasoline. This catalyst was premixed with 10 ml of a 1.6 M MAO/toluene solution (Schering) for 1 minute before the mixture was added to the reactor at a reactor temperature of 155 °C. The polymerisation was stopped after 7 minutes. Yield: 42.5 grams of polyethylene.
Example XVI
Ethylene polymerisation
Polymerisation as described in Example XV, but this time with using 1 ml of a 0.010 M suspension of the catalyst of Example XIII and 6.7 ml of a 1.6 M MAO/toluene solution (Schering). Yield: 34 grams of polyethylene.
Example XVII Ethylene polymerisation Polymerisation as described in Example XV, but this time with using 1 ml of a 0.015 M suspension of the catalyst of Example XIV and 10 ml of a 1.6 M MAO/toluene solution (Schering). Yield: 29 grams of polyethylene. Comparative Experiment H Ethylene polymerisation
Polymerisation as described in Example XV, but this time with 1 ml of a 0.015 M suspension of Cp2ZrCl2 and 10 ml of a 1.6 M MAO/toluene solution (Schering). Yield: 11.5 grams of polyethylene.
Comparative Experiment J Ethylene polymerisation Polymerisation as described in Example XV, but this time with 1 ml of a 0.015 M suspension of (l-Ind)2ZrCl2 and 10 ml of a 1.6 M MAO/toluene solution (Schering). Yield: 14.5 grams of polyethylene.
Example XVIII
Ethylene/propylene polymerisation
The reaction product of example XI was used for the solution copolymerisation of ethylene and propylene as described in Example VI. The Zr concentration in the reactor was 8 μmol/1; the feed temperature was 40 °C. This time the Al/Zr ratio was 1250. After 30 minutes' polymerisation, during which a maximum reaction temperature of 50 °C occurred, 35 grams of clear rubber without visible homopolymer by-product was isolated and worked up. The C3 content was 53 wt.%; the intrinsic viscosity was 0.1 dl/g.
Example XIX
Ethylene/propylene polymerisation The reaction product of example XII was used for the solution copolymerisation of ethylene and propylene as described in Example VI. This time 6 μmol Zr/1 was used and the Al/Zr ratio was 1670. The propylene/ethylene ratio in the gas phase was 6; the feed temperature 40 °C. After 30 minutes' polymerisation, during which a maximum reaction temperature of 46 °C occurred, 26 grams of clear rubber without visible homopolymer by-product was isolated and worked up. The C3 content of the product thus obtained was 62 wt.%; the intrinsic viscosity was 0.1 dl/g.
The products of Examples XVIII and XIX both had < 2% C3-inversions in the polymer chain.
Comparative Experiment K Ethylene/propylene polymerisation
Me2Si(3-Me-Cp)2ZrCl2 was used for the solution copolymerisation of ethylene and propylene as described in Example VI. The Al/Zr ratio was 2500. After 30 minutes' polymerisation, 5.2 grams of low-molecular-weight inhomogeneous product was isolated and worked up.
Comparative Experiment L
Ethylene/propylene polymerisation
In this experiment V0C13 was used as catalyst, in a concentration of 12.5 μmol/1. As cocatalyst, sesquiethyl aluminium chloride was used, in such an amount that the Al/V ratio was 16. As promoter, dichlorophenyl- acetic acid ethyl ester (DCPAE) was used, the DCPAE/V ratio being 4. A solution polymerisation of ethylene and propylene was carried out as described in Example VI. The propylene/ethylene ratio in the gas phase was 2 and the inlet temperature was 30 °C. After 10 minutes' polymerisation, during which a maximum reaction temperature of 40 °C occurred, the catalyst no longer showed any activity; 9 grams of clear rubber was obtained (Hoekstra 85). The C3 content of this rubber was 38 wt.%; the DSC measurement revealed a crystallization temperature of -6 °C.
Example XX
XX.1. Synthesis of methyl(2-indenyl)sulphide 11.0 grams of methanethiol was added to a solution of 13.7 grams of 2-indanone in 200 ml of chloroform. Next, a solution of 17.2 grams of trimethyl- chlorosilane in 30 ml of chloroform was added in 15 minutes, after which the mixture was stirred for 20 hours at room temperature. Thereafter, 25 ml of water was added dropwise, the mixture was extracted three times with 50 ml of a 10 wt.% sodiumhydroxide in water solution. The organic layer was evaporated; to the residu 150 ml of methanol and 15 drops of concentrated sulphuric acid were added. After a heating under reflux for 20 hours, 60 ml of water and 10 ml of a saturated sodiumbicarbonate solution were added. The methanol was evaporated, the remaining residue three times extracted with ether. The ether layers were dryed over MgS04. After evaporation, the remaining residue was purified over a silica column (mobile phase: gasoline/THF = 20/1). The yield was 10.98 grams (= 65%).
XX.2 Synthesis of bis(methyl(2-indenyl)sulphide)zirconium- dichloride
As in Example 1.2, this time with: 1.74 grams of methyl(2-indenyl)sulphide, 7.0 ml of n-BuLi solution,
1.25 grams of zirconiumtetrachloride.
After extraction with CH2C12, evaporation and drying 2.0 grams of a solid yellow compound, bis(methyl(2- indenyl)sulphide)zirconiumdichloride was obtained.
Example XXI
XXI.1. Synthesis of benzyl(2-indenyl)sulphide
To a solution of 2.77 grams of 2-indanone in 150 ml of chloroform, 5.40 grams of benzylthiol was added. Next, a solution of 4.27 grams of trimethylchlorosilane in 25 ml of chloroform was added in 30 minutes, after which the mixture was stirred for 90 hours at roomtemperature. The mixture was extracted three times with 30 ml of a 5 wt.% sodiumhydroxide in water solution, after which the organic layer was evaporated. The residu was dissolved in 150 ml of methanol and after addition of 10 drops of concentrated sulphuric acid, stirred for 2 hours under reflux. After cooling to room temperature, the crystallized product was filtered and dried. The yield was 2.91 grams (51%).
XXI.2. Synthesis of bis(benzyl(2-indenyl)sulphide)- zirconiumdichloride
As in Example XX.2, this time with: 1.46 grams of benzyl(2-indenyl)sulphide, 3.8 ml n-BuLi solution, 0.72 grams of zirconiumtetrachloride.
1.1 grams of the title compound was obtained (91%).
Example XXII XXII.1. Synthesis of n-butyl(2-indenyl)sulphide
19.3 grams of 1-butanethiol was added to a solution of 13.4 grams of 2-indanone in 200 ml of chloroform. Next, a solution of 23.5 grams of trimethylchlorosilane in 50 ml of chloroform was added in 30 minutes, after which the mixture was stirred for 65 hours at roomtemperature. Thereafter, 25 ml of water was added dropwise and the mixture extracted three times with 50 ml of a 5 wt.% sodiumhydroxide solution in water. The organic layer was dried over MgS04, evaporated and destilled under vacuum. The residue was dissolved in 150 ml of methanol; 15 drops of concentrated sulphuric acid were added and refluxed for 2 hours. After cooling to room temperature, 10 ml of a NH3-solution was added; methanol was evaporated; 50 ml of water was added to the residu. After 3 extractions with ether, the etherlayers were dryed over MgS04 and evaporated. The yield was 10.7 grams (52%).
XXII.2. Synthesis of bis(n-butyl(2-indenyl)sulphide)- zirconiumdichloride As in Example XX.2, this time with:
4.51 grams of n-butyl(2-indenyl)sulphide, 13.8 mol n-BuLi-solution, 2.57 grams of zirconiumtetrachloride.
2.0 grams of a yellow powder of the title compound (32%) was obtained.
Example XXIII
XXIII.1. Synthesis of phenyl(2-indenyl)sulphide
17.7 grams of thiophenol was added to a solution of 10.2 grams of 2-indanon in 200 ml of chloroform. Next, a solution of 16.9 grams of trimethylchlorosilane in 50 ml of chloroform was added in 30 minutes, after which the mixture was stirred for 65 hours at roomtemperature. Thereafter, the mixture was extracted three times with 50 ml of a 5 wt.% sodiumhydroxide in water solution, after which the organic layer was evaporated. To the residue 250 ml of methanol and 25 drops of concentrated sulphuric acid was added and the mixture heated for two hours under reflux. After evaporation, the remaining residue was purified over a silica column (mobile phase: hexane/THF = 20/1). The yield was 7.84 grams (45%).
XXIII.2. Synthesis of bis(phenyl(2-indenyl)sulphide)- zirconiumdichloride
As in Example XX.2, this time with: 2.31 grams of phenyl(2-indenyl)sulphide, 6.4 ml n-BuLi-solution,
1.26 grams of zirconiumtetrachloride.
2.1 grams of a yellow powder of the title compound (66%) was obtained.
Examples XXIV to XXVII Ethylene polymerisation
In the following examples, a 1.5 1 reactor was filled with 450 ml of gasoline, pressurized with ethylene and brought to reaction condition (50 °C; pressure = 0.7 MPa). To the reactor was added 3.3 ml of MAO (1.6 M in toluene). 25 ml of gasoline and 0.25 ml of a 0.01 M solution of a 2-indenyl compound were mixed and added to the reactor. An after-rinse was performed with 25 ml of gasoline. After 7 minutes of polymerisation at 50 °C and 0.7 MPa, the polymerisation was stopped by releasing the pressure to atmospheric pressure and the polyethylene was isolated and dried. The respective 2-indenyl compounds used are the compounds of Examples XX to XXIII. The polymerisation results are given in the following table:
Figure imgf000037_0001
* Result: grams of polyethylene obtained
** Yield: expressed in kg polyethylene/grams transition metal.5 minutes

Claims

C L I M S
1. Indenyl compound of the general formula:
R'Ind-M-(Cp)-Qk (1)
in which the symbols have the following meanings:
Ind an indenyl group
R' a substituent, other than hydrogen, to the Ind group
Cp a cyclopentadienyl group
M a transition metal from group 3, 4, 5 or 6 of the Periodic System of Elements
0 a ligand to M and k is an integer linked to the valence of M, characterized in that R' is bound to the Ind group at the 2-position; compounds in which the Cp-group is an indenyl group and in which either: a) the Ind- and the Cp-groups are bridged over the respective 1-positions, or b) the indenyl compound is bis(2,3-dimethyl-l- indenyl)zirconiumdichloride, or c) the indenyl compound is either ethylene-l-(3- but-3-enyl)inden-1-yl)-2-( (l-but-3-enyl)-inden- 2-yl)-zirconiumdichloride, or ethylene-1-( (3-allyldimethylsilyl)inden-1-yl)-2- ( (l-allyldimethylsilyl)inden-2-yl)zirconium- dichloride, are disclaimed.
2. Indenyl compound according to Claim 1, characterized in that R' is an alkyl group.
3. Indenyl compound according to Claim 2, characterized in that the alkyl group contains 1-4 carbon atoms.
4. Indenyl compound according to any one of Claims 1-3, characterized in that the Cp group is a 2-indenyl group with the formula: R"Ind where R" is a substituent other than hydrogen at the
2-position of the Ind group.
5. Indenyl compound according to Claim 4, characterized in that the R" group is an alkyl group.
6. Indenyl compound according to Claim 5, characterized in that the alkyl group R" contains 1-4 carbon atoms.
7. Indenyl compound according to Claim 1, characterized in that R' forms a bridge between the Ind group and the Cp group in formula (1).
8. Indenyl compound according to Claim 7, characterized in that the indenyl compound is of the formula:
Figure imgf000039_0001
where R is bound at the 2-position to both 2-Ind groups.
9. Indenyl compound according to Claim 8, characterized in that R is chosen from a methylydene group, an ethylydene group or a group with at least one heteroatom from group 14, 15 or 16 of the Periodic System of Elements.
10. Indenyl compound according to Claim 9, in which R contains a heteroatom, characterized in that this heteroatom is chosen from the group comprising silicon, nitrogen, phosphorus, oxygen and sulphur.
11. Catalyst component for the polymerisation of olefins comprising a 2-indenyl compound according to any one of Claims 1-10.
12. Process for the polymerisation of an olefin, in which an indenyl compound, optionally in the presence of a cocatalyst, is contacted with an olefin, characterized in that the indenyl compound is a 2- indenyl compound according to any one of Claims 1-10.
13. Process according to Claim 12, characterized in that the olefin is chosen from the group comprising α-olefin, internal olefin, diolefin and mixtures thereof.
14. Process according to Claim 13, characterized in that the α-olefin is chosen from the group comprising ethylene, propylene, butene, pentene, heptene, octene or mixtures thereof.
15. Process according to any one of Claims 12-14, characterized in that a polymer is prepared on the basis of ethylene and/or propylene.
16. Process according to Claim 15, characterized in that a rubbery polymer is prepared on the basis of ethylene, propylene and, optionally, a diene.
17. Polyolefin obtainable by a process according to any one of Claims 12-16.
18. Rubbery polymer of ethylene, an α-olefin and, optionally, a diene, characterized in that the number of α-olefine inversions in the polymer is 0-5%.
PCT/NL1993/000229 1992-11-11 1993-11-03 Indenyl compounds and catalyst components for the polymerization of olefins WO1994011406A1 (en)

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Cited By (35)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995016716A1 (en) * 1993-12-14 1995-06-22 Exxon Chemical Patents Inc. Process for producing elastomers with an indenyl metallocene catalyst system
WO1995030698A1 (en) * 1994-05-06 1995-11-16 Dsm N.V. Process for the preparation of an elastomeric polymer from ethylene, alpha-olefin and optionally diene
EP0685485A1 (en) * 1994-06-03 1995-12-06 Phillips Petroleum Company High activity ethylene selective metallocenes
EP0693502A1 (en) * 1994-07-22 1996-01-24 Mitsubishi Chemical Corporation Catalyst component for the polymerization of alpha-olefins and a process for preparing alpha-olefin polymers with use of same
EP0693506A2 (en) 1994-07-20 1996-01-24 SPHERILENE S.p.A. Process for the preparation of amorphous polymers of propylene
US5491207A (en) * 1993-12-14 1996-02-13 Exxon Chemical Patents Inc. Process of producing high molecular weight ethylene-α-olefin elastomers with an indenyl metallocene catalyst system
US5594080A (en) * 1994-03-24 1997-01-14 Leland Stanford, Jr. University Thermoplastic elastomeric olefin polymers, method of production and catalysts therefor
ES2116188A1 (en) * 1994-12-30 1998-07-01 Repsol Quimica Sa Process for obtaining polyolefins with broad bimodal or multimodal molecular weight distributions
US5780659A (en) * 1996-03-29 1998-07-14 Phillips Petroleum Company Substituted indenyl unbridged metallocenes
NL1006346C2 (en) * 1997-06-18 1998-12-21 Dsm Nv Process for the preparation of high temperature polyolefins using Zr metallocenes.
EP0940412A1 (en) * 1998-03-04 1999-09-08 Bayer Aktiengesellschaft Atactic propylene (co)polymers
EP0940408A1 (en) * 1998-03-04 1999-09-08 Bayer Aktiengesellschaft Metalorganic compounds
EP0941997A2 (en) * 1998-03-09 1999-09-15 Montell Technology Company bv Bridged zirconocene compounds, process for their preparation, and their use as catalyst components in the polymerization of olefins
EP1033371A1 (en) * 1999-03-02 2000-09-06 TARGOR GmbH Transition metal compound, catalyst system, process for the preparation thereof and its use for the polymerization of olefins
EP1059300A1 (en) * 1999-06-11 2000-12-13 Dsm N.V. Indenyl compounds for the polymerisation of olefins
EP1059299A1 (en) * 1999-06-11 2000-12-13 Dsm N.V. Indenyl compounds for the polymerisation of olefins
US6232484B1 (en) 1998-03-09 2001-05-15 Montell Technology B.V. Bridged zirconocene compounds, process for their preparation and their use as catalyst components in the polymerization of olefins
CN1065869C (en) * 1997-01-08 2001-05-16 菲利浦石油公司 (organo) ((omega-alkenyl) cyclopentacarbyl) (silane-bridged) metallocene compounds
EP1120424A2 (en) * 2000-01-28 2001-08-01 Bayer Ag Organometallic compounds with annelated indenyl ligands
US6355819B1 (en) 1997-04-14 2002-03-12 Borealis Technology Oy Substituted metallocene compounds for olefin polymerization catalyst systems, their intermediates and methods for preparing them
US6369254B1 (en) 1995-05-30 2002-04-09 Basell Technology Company Bv Bridged metallocene compounds, processes for the preparation thereof and use thereof in catalysts for the polymerization of olefins
WO2003008465A2 (en) * 2001-07-19 2003-01-30 Univation Technologies, Llc Low comonomer incorporating metallocene catalyst compounds
US6541584B1 (en) 1998-11-18 2003-04-01 Basell Poliolefine Italia S.P.A. Bis(tetrahydro-indenyl) metallocenes as olefin-polymerization-catalyst
US6545088B1 (en) 1991-12-30 2003-04-08 Dow Global Technologies Inc. Metallocene-catalyzed process for the manufacture of EP and EPDM polymers
US6693156B1 (en) 1998-11-18 2004-02-17 Basell Polyolefine Gmbh Methylene bridged metallocenes as olefin-polymerization-catalyst components
US6984703B1 (en) * 1999-12-03 2006-01-10 Polimeri Europa S.P.A. Bridged metallocene compounds as olefin-polymerization catalysts
US9815917B2 (en) 2013-08-30 2017-11-14 Saudi Basic Industries Corporation Bridged metallocene complex for olefin polymerization
US9868797B2 (en) 2013-08-01 2018-01-16 Saudi Basic Industries Corporation Bridged metallocene complex for olefin polymerization
WO2018185170A1 (en) 2017-04-04 2018-10-11 Sabic Global Technologies B.V. Dihydrocarbyl-silyl-bridged-1.3 disubstituted-2-indenyl metallocene complexes for olefin polymerization
WO2018185176A1 (en) 2017-04-04 2018-10-11 Sabic Global Technologies B.V. Dihydrocarbyl-silyl-bridged-substituted cyclopentadienyl metallocene complexes for olefin polymerization
WO2018185173A1 (en) 2017-04-04 2018-10-11 Sabic Global Technologies B.V. Dimethyl-silyl-bridged-1-substituted-2-indenyl metallocene complexes for olefin polymerization
WO2019122459A1 (en) 2017-12-22 2019-06-27 Sabic Global Technologies B.V. Process for preparation of functionalized ethylene and propylene copolymer
WO2019122455A1 (en) 2017-12-22 2019-06-27 Sabic Global Technologies B.V. Process for preparation of amorphous functionalized olefin copolymer
WO2019145371A1 (en) 2018-01-24 2019-08-01 Sabic Global Technologies B.V. 1,2-phenylene bridged 1-indenyl-2-indenyl metallocene complexes for olefin polymerisation
WO2021173361A1 (en) * 2020-02-24 2021-09-02 Exxonmobil Chemical Patents Inc. Ansa-bis(inden-2-yl) catalysts for producing vinylidene-terminated polyalphaolefins

Families Citing this family (33)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL9201970A (en) * 1992-11-11 1994-06-01 Dsm Nv Indenyl compounds and catalyst components for the polymerization of olefins.
DE60036158T2 (en) * 1999-01-21 2008-05-21 Boulder Scientific Co., Mead SYNTHESIS AND ISOMERIZATION OF 1,2-BIS (INDENYL) ETHANTS
US6342622B1 (en) 1999-06-11 2002-01-29 Dsm B.V. Indenyl compounds for the polymerization of olefins
US6482905B1 (en) * 1999-08-16 2002-11-19 Phillips Petroleum Company Unsymmetric unbridged bis-indenyl metallocenes and their use
DE10127926A1 (en) 2001-06-08 2002-12-12 Bayer Ag 1,3-disubstituted indene complexes
WO2003008468A2 (en) 2001-07-19 2003-01-30 Univation Technologies, Llc Mixed metallocene catalyst systems containing a poor comonomer incorporator and a good comonomer incorporator
US6956088B2 (en) * 2001-07-19 2005-10-18 Univation Technologies, Llc Polyethylene films with improved physical properties
US6936675B2 (en) * 2001-07-19 2005-08-30 Univation Technologies, Llc High tear films from hafnocene catalyzed polyethylenes
US6562921B1 (en) * 2001-10-12 2003-05-13 Univation Technologies, Llc Catalyst precursor compound and olefin polymerization process using same
ATE361323T1 (en) * 2004-03-12 2007-05-15 Saudi Basic Ind Corp CATALYST COMPOSITION FOR THE POLYMERIZATION OF OLEFINS AND POLYMERIZATION PROCESSES USING SAME
US7312283B2 (en) * 2005-08-22 2007-12-25 Chevron Phillips Chemical Company Lp Polymerization catalysts and process for producing bimodal polymers in a single reactor
US7226886B2 (en) 2005-09-15 2007-06-05 Chevron Phillips Chemical Company, L.P. Polymerization catalysts and process for producing bimodal polymers in a single reactor
US7619047B2 (en) * 2006-02-22 2009-11-17 Chevron Phillips Chemical Company, Lp Dual metallocene catalysts for polymerization of bimodal polymers
WO2013091836A1 (en) * 2011-12-19 2013-06-27 Saudi Basic Industries Corporation (Sabic) Process for the preparation of metallocene complexes
EP2800754B1 (en) * 2011-12-19 2017-06-28 Saudi Basic Industries Corporation (Sabic) Process for the preparation of metallocene complexes
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US8937139B2 (en) 2012-10-25 2015-01-20 Chevron Phillips Chemical Company Lp Catalyst compositions and methods of making and using same
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US9034991B2 (en) 2013-01-29 2015-05-19 Chevron Phillips Chemical Company Lp Polymer compositions and methods of making and using same
KR101584350B1 (en) * 2013-04-08 2016-01-13 한화케미칼 주식회사 Metallocene catalyst system comprising antistatic agents and method for preparing polyolefin using the same
WO2014168373A1 (en) * 2013-04-08 2014-10-16 Hanwha Chemical Corporation Metallocene catalyst system comprising antistatic agent and method for preparing polyolefin using the same
ES2944883T3 (en) 2014-02-11 2023-06-26 Univation Tech Llc Production of polyolefin products
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EP3034546B1 (en) 2014-12-17 2019-10-16 SABIC Global Technologies B.V. A process for the preparation of a block copolymer comprising a first polyolefin block and a second polymer block
EP3034545B1 (en) 2014-12-17 2020-11-04 SABIC Global Technologies B.V. A process for the preparation of a graft copolymer comprising a polyolefin main chain and one or a multiple polymer side chains and the products obtained therefrom
EP3037438A1 (en) 2014-12-23 2016-06-29 SABIC Global Technologies B.V. Process for the preparation of a branched polyolefin
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KR102064412B1 (en) 2016-07-07 2020-01-09 주식회사 엘지화학 Preparation method of metallocene catalyst for preparing polyolefin
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WO2021048030A1 (en) 2019-09-10 2021-03-18 Sabic Global Technologies B.V. Compounds for use in catalyst compositions for the production of polyolefins
US20220356275A1 (en) 2019-09-20 2022-11-10 Sabic Global Technologies B.V. Compounds for use in catalyst compositions for the production of polyolefins

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0344887A2 (en) * 1988-03-21 1989-12-06 Exxon Chemical Patents Inc. Silicon bridged transition metal compounds
EP0372414A2 (en) * 1988-12-03 1990-06-13 Hoechst Aktiengesellschaft Method for the preparation of a metallocene component of a heterogeneous catalyst
EP0485823A1 (en) * 1990-11-12 1992-05-20 Hoechst Aktiengesellschaft 2-Substituted bisindenyl-metallocenes, process for their preparation and their use as catalysts for the polymerization of olefins
EP0485821A1 (en) * 1990-11-12 1992-05-20 Hoechst Aktiengesellschaft Metallocenes with 2-substituted indenyl-derivates as ligands, process for their preparation and their use as catalysts
EP0500944A1 (en) * 1990-07-24 1992-09-02 MITSUI TOATSU CHEMICALS, Inc. CATALYST FOR $g(a)-OLEFIN POLYMERIZATION AND PRODUCTION OF POLY-$g(a)-OLEFIN THEREWITH

Family Cites Families (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2322883A1 (en) * 1975-09-02 1977-04-01 Michelin & Cie ELASTOMERS OF THE E P T TYPE, AND ARTICLES CONTAINING SUCH ELASTOMERS
CA1257863A (en) * 1985-10-17 1989-07-25 Vaclav G. Zboril SOLUTION PROCESS FOR THE PREPARATION OF POLYMERS OF .alpha.-OLEFINS
ATE114678T1 (en) * 1986-09-24 1994-12-15 Mitsui Petrochemical Ind PROCESSES FOR POLYMERIZATION OF POLYOLEFINS.
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
US5055438A (en) * 1989-09-13 1991-10-08 Exxon Chemical Patents, Inc. Olefin polymerization catalysts
US5120867A (en) * 1988-03-21 1992-06-09 Welborn Jr Howard C Silicon-bridged transition metal compounds
US5017714A (en) * 1988-03-21 1991-05-21 Exxon Chemical Patents Inc. Silicon-bridged transition metal compounds
US4871705A (en) * 1988-06-16 1989-10-03 Exxon Chemical Patents Inc. Process for production of a high molecular weight ethylene a-olefin elastomer with a metallocene alumoxane catalyst
US5001205A (en) * 1988-06-16 1991-03-19 Exxon Chemical Patents Inc. Process for production of a high molecular weight ethylene α-olefin elastomer with a metallocene alumoxane catalyst
KR930002411B1 (en) * 1988-09-14 1993-03-30 미쓰이세끼유 가가꾸고오교오 가부시끼가이샤 Benzene-insoluble organoalumium oxy-compounds and process for preparing same
WO1991002012A1 (en) * 1989-08-03 1991-02-21 Exxon Chemical Patents Inc. Very high molecular weight polyethylene
US5191042A (en) * 1989-09-06 1993-03-02 Exxon Chemical Patents Inc. Process for preparing alpha-olefin copolymers having a narrow MWD and broad compositional distribution
ATE137770T1 (en) * 1989-10-10 1996-05-15 Fina Technology METALLOCENE CATALYST WITH LEWISS ACID AND ALKYL ALUMINUM
US5098635A (en) * 1989-11-09 1992-03-24 Copolymer Rubber & Chemical Corporation Process for manufacturing friable rubber bales
ATE122688T1 (en) * 1990-01-02 1995-06-15 Exxon Chemical Patents Inc SUPPORTED IONIC METALLOCE CATALYSTS FOR OLEFIN POLYMERIZATION.
DE4039451A1 (en) * 1990-12-11 1992-06-17 Hoechst Ag METALLOCENES WITH BICYCLIC CYCLOPENTADIENE DERIVATIVES AS LIGANDS, METHOD FOR THE PRODUCTION THEREOF AND THEIR USE AS CATALYSTS
ES2155492T3 (en) * 1991-05-27 2001-05-16 Basell Polyolefine Gmbh PROCEDURE FOR OBTAINING POLYOLEFINS WITH A LARGE DISTRIBUTION OF MOLECULAR WEIGHTS.
US5391789A (en) * 1991-08-08 1995-02-21 Hoechst Aktiengesellschaft Bridged, chiral metallocenes, processes for their preparation and their use as catalysts
DE4139261A1 (en) * 1991-11-29 1993-06-03 Basf Ag LOW DENSITY ETHYLENE COPOLYMERISATE
ES2100388T3 (en) * 1992-05-26 1997-06-16 Hoechst Ag PROCEDURE FOR PREPARING POLYOLEFIN WAXES.
ES2114978T3 (en) * 1992-08-03 1998-06-16 Targor Gmbh PROCEDURE FOR OBTAINING AN OLEPHINE POLYMER UNDER THE USE OF METALLOCES WITH SPECIAL SUBSTITUTION INDENYL LIGANDS.
NL9201970A (en) * 1992-11-11 1994-06-01 Dsm Nv Indenyl compounds and catalyst components for the polymerization of olefins.
US5372980A (en) * 1993-06-03 1994-12-13 Polysar Bimetallic metallocene alumoxane catalyst system and its use in the preparation of ethylene-alpha olefin and ethylene-alpha olefin-non-conjugated diolefin elastomers
DE4344689A1 (en) * 1993-12-27 1995-06-29 Hoechst Ag Metallocene compound
DE4344688A1 (en) * 1993-12-27 1995-06-29 Hoechst Ag Metallocene compound

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0344887A2 (en) * 1988-03-21 1989-12-06 Exxon Chemical Patents Inc. Silicon bridged transition metal compounds
EP0372414A2 (en) * 1988-12-03 1990-06-13 Hoechst Aktiengesellschaft Method for the preparation of a metallocene component of a heterogeneous catalyst
EP0500944A1 (en) * 1990-07-24 1992-09-02 MITSUI TOATSU CHEMICALS, Inc. CATALYST FOR $g(a)-OLEFIN POLYMERIZATION AND PRODUCTION OF POLY-$g(a)-OLEFIN THEREWITH
EP0485823A1 (en) * 1990-11-12 1992-05-20 Hoechst Aktiengesellschaft 2-Substituted bisindenyl-metallocenes, process for their preparation and their use as catalysts for the polymerization of olefins
EP0485821A1 (en) * 1990-11-12 1992-05-20 Hoechst Aktiengesellschaft Metallocenes with 2-substituted indenyl-derivates as ligands, process for their preparation and their use as catalysts

Cited By (69)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6545088B1 (en) 1991-12-30 2003-04-08 Dow Global Technologies Inc. Metallocene-catalyzed process for the manufacture of EP and EPDM polymers
US5491207A (en) * 1993-12-14 1996-02-13 Exxon Chemical Patents Inc. Process of producing high molecular weight ethylene-α-olefin elastomers with an indenyl metallocene catalyst system
WO1995016716A1 (en) * 1993-12-14 1995-06-22 Exxon Chemical Patents Inc. Process for producing elastomers with an indenyl metallocene catalyst system
US5594080A (en) * 1994-03-24 1997-01-14 Leland Stanford, Jr. University Thermoplastic elastomeric olefin polymers, method of production and catalysts therefor
WO1995030698A1 (en) * 1994-05-06 1995-11-16 Dsm N.V. Process for the preparation of an elastomeric polymer from ethylene, alpha-olefin and optionally diene
NL9400758A (en) * 1994-05-06 1995-12-01 Dsm Nv Process for the preparation of a high molecular weight polymer from ethylene, alpha olefin and optionally diene.
EP0685485A1 (en) * 1994-06-03 1995-12-06 Phillips Petroleum Company High activity ethylene selective metallocenes
CN1050612C (en) * 1994-06-03 2000-03-22 菲利浦石油公司 High activity ethylene selective metallocenes
EP0693506A2 (en) 1994-07-20 1996-01-24 SPHERILENE S.p.A. Process for the preparation of amorphous polymers of propylene
EP0693506A3 (en) * 1994-07-20 1998-04-08 Montell Technology Company bv Process for the preparation of amorphous polymers of propylene
US6391991B1 (en) 1994-07-20 2002-05-21 Basell Technology Company Bv Process for the preparation of amorphous polymers of propylene
EP0693502A1 (en) * 1994-07-22 1996-01-24 Mitsubishi Chemical Corporation Catalyst component for the polymerization of alpha-olefins and a process for preparing alpha-olefin polymers with use of same
ES2116188A1 (en) * 1994-12-30 1998-07-01 Repsol Quimica Sa Process for obtaining polyolefins with broad bimodal or multimodal molecular weight distributions
US6369254B1 (en) 1995-05-30 2002-04-09 Basell Technology Company Bv Bridged metallocene compounds, processes for the preparation thereof and use thereof in catalysts for the polymerization of olefins
SG96172A1 (en) * 1996-03-29 2003-05-23 Phillips Petroleum Co Substituted indenyl unbridges metallocenes
US6037427A (en) * 1996-03-29 2000-03-14 Schmid; Claudia Polymerization with substituted indenyl cyclopentadienyl metallocenes
US5780659A (en) * 1996-03-29 1998-07-14 Phillips Petroleum Company Substituted indenyl unbridged metallocenes
CN1065869C (en) * 1997-01-08 2001-05-16 菲利浦石油公司 (organo) ((omega-alkenyl) cyclopentacarbyl) (silane-bridged) metallocene compounds
US6355819B1 (en) 1997-04-14 2002-03-12 Borealis Technology Oy Substituted metallocene compounds for olefin polymerization catalyst systems, their intermediates and methods for preparing them
NL1006346C2 (en) * 1997-06-18 1998-12-21 Dsm Nv Process for the preparation of high temperature polyolefins using Zr metallocenes.
WO1998057997A1 (en) * 1997-06-18 1998-12-23 Dsm N.V. PROCESS FOR PREPARING POLYOLEFINS AT A HIGH TEMPERATURE WITH THE AID OF Zr METALLOCENES
EP0940412A1 (en) * 1998-03-04 1999-09-08 Bayer Aktiengesellschaft Atactic propylene (co)polymers
EP0940408A1 (en) * 1998-03-04 1999-09-08 Bayer Aktiengesellschaft Metalorganic compounds
EP0941997A3 (en) * 1998-03-09 2000-06-14 Montell Technology Company bv Bridged zirconocene compounds, process for their preparation, and their use as catalyst components in the polymerization of olefins
US6673880B2 (en) 1998-03-09 2004-01-06 Basell Technology Company B.V. Bridged zirconocene compounds, process for their preparation and their use as catalyst components in the polymerization of olefins
US6306791B2 (en) 1998-03-09 2001-10-23 Basell Technology Company Bv Bridged zirconocene compounds, process for their preparation and their use as catalyst components in the polymerization of olefins
US6232484B1 (en) 1998-03-09 2001-05-15 Montell Technology B.V. Bridged zirconocene compounds, process for their preparation and their use as catalyst components in the polymerization of olefins
EP0941997A2 (en) * 1998-03-09 1999-09-15 Montell Technology Company bv Bridged zirconocene compounds, process for their preparation, and their use as catalyst components in the polymerization of olefins
US6693156B1 (en) 1998-11-18 2004-02-17 Basell Polyolefine Gmbh Methylene bridged metallocenes as olefin-polymerization-catalyst components
US6872863B2 (en) 1998-11-18 2005-03-29 Basell Polyolefine Gmbh Methylene bridged metallocenes as olefin-polymerization catalyst components
US6541584B1 (en) 1998-11-18 2003-04-01 Basell Poliolefine Italia S.P.A. Bis(tetrahydro-indenyl) metallocenes as olefin-polymerization-catalyst
EP1033371A1 (en) * 1999-03-02 2000-09-06 TARGOR GmbH Transition metal compound, catalyst system, process for the preparation thereof and its use for the polymerization of olefins
US6458982B1 (en) 1999-03-02 2002-10-01 Targor Gmbh Transition metal compound, catalyst, its production and its use for the polymerization of olefins
EP1059300A1 (en) * 1999-06-11 2000-12-13 Dsm N.V. Indenyl compounds for the polymerisation of olefins
EP1059299A1 (en) * 1999-06-11 2000-12-13 Dsm N.V. Indenyl compounds for the polymerisation of olefins
US6984703B1 (en) * 1999-12-03 2006-01-10 Polimeri Europa S.P.A. Bridged metallocene compounds as olefin-polymerization catalysts
EP1120424A3 (en) * 2000-01-28 2002-10-16 Bayer Ag Organometallic compounds with annelated indenyl ligands
US6613713B2 (en) 2000-01-28 2003-09-02 Bayer Aktiengesellschaft Organometallic compounds with fused indenyl ligands
EP1120424A2 (en) * 2000-01-28 2001-08-01 Bayer Ag Organometallic compounds with annelated indenyl ligands
US7060765B2 (en) 2001-07-19 2006-06-13 Univation Technologies, Llc Low comonomer incorporating metallocene catalyst compounds
WO2003008465A2 (en) * 2001-07-19 2003-01-30 Univation Technologies, Llc Low comonomer incorporating metallocene catalyst compounds
WO2003008465A3 (en) * 2001-07-19 2003-08-28 Univation Tech Llc Low comonomer incorporating metallocene catalyst compounds
US9868797B2 (en) 2013-08-01 2018-01-16 Saudi Basic Industries Corporation Bridged metallocene complex for olefin polymerization
US10513569B2 (en) 2013-08-30 2019-12-24 Saudi Basic Industries Corporation Bridged metallocene complex for olefin polymerization
US9815917B2 (en) 2013-08-30 2017-11-14 Saudi Basic Industries Corporation Bridged metallocene complex for olefin polymerization
WO2018185170A1 (en) 2017-04-04 2018-10-11 Sabic Global Technologies B.V. Dihydrocarbyl-silyl-bridged-1.3 disubstituted-2-indenyl metallocene complexes for olefin polymerization
WO2018185176A1 (en) 2017-04-04 2018-10-11 Sabic Global Technologies B.V. Dihydrocarbyl-silyl-bridged-substituted cyclopentadienyl metallocene complexes for olefin polymerization
WO2018185173A1 (en) 2017-04-04 2018-10-11 Sabic Global Technologies B.V. Dimethyl-silyl-bridged-1-substituted-2-indenyl metallocene complexes for olefin polymerization
US11427608B2 (en) 2017-04-04 2022-08-30 Sabic Global Technologies B.V. Dihydrocarbyl-silyl-bridged-1,3 disubstituted-2-indenyl metallocene complexes for olefin polymerization
US11352386B2 (en) 2017-04-04 2022-06-07 Sabic Global Technologies B.V. Dihydrocarbyl-silyl-bridged-substituted cyclopentadienyl metallocene complexes for olefin polymerization
US11155659B2 (en) 2017-04-04 2021-10-26 Sabic Global Technologies B.V. Dimethyl-silyl-bridged-1-substituted-2-indenyl metallocene complexes for olefin polymerization
WO2019122459A1 (en) 2017-12-22 2019-06-27 Sabic Global Technologies B.V. Process for preparation of functionalized ethylene and propylene copolymer
WO2019122457A1 (en) 2017-12-22 2019-06-27 Sabic Global Technologies B.V. Process for preparation of ethylene and propylene ionomer
US11773195B2 (en) 2017-12-22 2023-10-03 Sabic Global Technologies B.V. Process for preparation of semi-crystalline functionalized olefin copolymer
WO2019122458A1 (en) 2017-12-22 2019-06-27 Sabic Global Technologies B.V. Process for preparation of semi-crystalline polyolefinic ionomers
US11472900B2 (en) 2017-12-22 2022-10-18 Sabic Global Technologies B.V. Process for preparation of ethylene and propylene ionomer
WO2019122453A1 (en) 2017-12-22 2019-06-27 Sabic Global Technologies B.V. Process for preparation of amorphous polyolefinic ionomers
WO2019122456A1 (en) 2017-12-22 2019-06-27 Sabic Global Technologies B.V. Process for preparation of semi-crystalline functionalized olefin copolymer
US11396565B2 (en) 2017-12-22 2022-07-26 Sabic Global Technologies B.V. Process for preparation of semi-crystalline functionalized olefin copolymer
US11401360B2 (en) 2017-12-22 2022-08-02 Sabic Global Technologies B.V. Process for preparation of amorphous polyolefinic ionomers
WO2019122455A1 (en) 2017-12-22 2019-06-27 Sabic Global Technologies B.V. Process for preparation of amorphous functionalized olefin copolymer
US11447585B2 (en) 2017-12-22 2022-09-20 Sabic Global Technologies B.V. Process for preparation of functionalized ethylene and propylene copolymer
US11466109B2 (en) 2017-12-22 2022-10-11 Sabic Global Technologies B.V. Process for preparation of amorphous functionalized olefin copolymer
US11466110B2 (en) 2017-12-22 2022-10-11 Sabic Global Technologies B.V. Process for preparation of semi-crystalline polyolefinic ionomers
US11691998B2 (en) 2018-01-24 2023-07-04 Sabic Global Technologies B.V. 1,2-phenylene bridged 1-indenyl-2-indenyl metallocene complexes for olefin polymerisation
WO2019145371A1 (en) 2018-01-24 2019-08-01 Sabic Global Technologies B.V. 1,2-phenylene bridged 1-indenyl-2-indenyl metallocene complexes for olefin polymerisation
WO2021173361A1 (en) * 2020-02-24 2021-09-02 Exxonmobil Chemical Patents Inc. Ansa-bis(inden-2-yl) catalysts for producing vinylidene-terminated polyalphaolefins
CN115485311A (en) * 2020-02-24 2022-12-16 埃克森美孚化学专利公司 Ansa-bis (inden-2-yl) catalysts for the production of vinylidene-terminated polyalphaolefins
US11613593B2 (en) 2020-02-24 2023-03-28 Exxonmobil Chemical Patents Inc. Ansa-bis(inden-2-yl) catalysts for producing vinylidene-terminated polyalphaolefins

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