WO1994012547A2 - Polymerisation de monomeres fonctionnalises a l'aide de catalyseurs de ziegler-natta - Google Patents

Polymerisation de monomeres fonctionnalises a l'aide de catalyseurs de ziegler-natta Download PDF

Info

Publication number
WO1994012547A2
WO1994012547A2 PCT/US1993/011186 US9311186W WO9412547A2 WO 1994012547 A2 WO1994012547 A2 WO 1994012547A2 US 9311186 W US9311186 W US 9311186W WO 9412547 A2 WO9412547 A2 WO 9412547A2
Authority
WO
WIPO (PCT)
Prior art keywords
radicals
aryl
structural formula
alkyl radical
following structural
Prior art date
Application number
PCT/US1993/011186
Other languages
English (en)
Other versions
WO1994012547A3 (fr
Inventor
Robert M. Waymouth
Michael R. Kesti
Geoffrey W. Coates
Original Assignee
The Board Of Trustees Of The Leland Stanford Junior University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by The Board Of Trustees Of The Leland Stanford Junior University filed Critical The Board Of Trustees Of The Leland Stanford Junior University
Priority to EP94902289A priority Critical patent/EP0623149A4/en
Priority to JP6513242A priority patent/JPH07507095A/ja
Publication of WO1994012547A2 publication Critical patent/WO1994012547A2/fr
Publication of WO1994012547A3 publication Critical patent/WO1994012547A3/fr

Links

Classifications

    • 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
    • C08F36/00Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds
    • C08F36/02Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds
    • C08F36/20Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, at least one having two or more carbon-to-carbon double bonds the radical having only two carbon-to-carbon double bonds unconjugated
    • 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
    • C08F10/14Monomers containing five or more carbon atoms
    • 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
    • C08F4/64Titanium, zirconium, hafnium or compounds thereof
    • C08F4/659Component covered by group C08F4/64 containing a transition metal-carbon bond
    • C08F4/6592Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring
    • C08F4/65922Component covered by group C08F4/64 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
    • C08F4/65925Component covered by group C08F4/64 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 two cyclopentadienyl rings being mutually non-bridged
    • 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
    • C08F4/64Titanium, zirconium, hafnium or compounds thereof
    • C08F4/659Component covered by group C08F4/64 containing a transition metal-carbon bond
    • C08F4/6592Component covered by group C08F4/64 containing a transition metal-carbon bond containing at least one cyclopentadienyl ring, condensed or not, e.g. an indenyl or a fluorenyl ring
    • C08F4/65922Component covered by group C08F4/64 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
    • C08F4/65927Component covered by group C08F4/64 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 two cyclopentadienyl rings being mutually bridged

Definitions

  • the invention relates to functionalized polyolefins and particularly to methods of polymerizing alpha-olefins containing functional groups.
  • poly(alpha-olefins) has been an area of long-standing interest as it represents a useful method for modifying the chemical and physical properties of poly(alpha- olefins).
  • Commercially useful improvements in the adhesive, thermal, rheological, morphological, and mechanical properties of the polymer can be achieved by introducing functionality onto the polymer.
  • polyolefin polymers containing functional groups show improved affinity for dyes and printing agents and are more compatible with polar polymers.
  • Post-polymerization functionalization techniques include free-radical grafting of unsaturated groups onto the polymer (Mukherjee et al., J. Macromol . Sci . Chem. , A19 (1983), p. 1069), polymer oxidation (Dasgupta, S., J. Appl . Polym. Sci . , 41 (1990), p. 233), anionic treatment of the polymer (Harada et al., Jpn Kokai Tokkyo Koho JP 62054713), and high energy radiation of the polymer (Stamm et al., J. Appl . Polym. Sci . , 7 (1963), p. 753).
  • catalyst systems employing a cationic Group 4 metallocene and "compatible non-coordinating anions.”
  • New generation Ziegler-Natta type catalysts also includes catalysts based on Group 4 metallocenes and methylaluminoxane cocatalysts. These "new generation” catalysts are superior to the conventional catalysts for the polymerization of functionalized monomers and the copolymerization of functionalized monomers with alpha-olefins.
  • One aspect of the present invention is the choice of functional monomer to be polymerized with the new generation "cationic" metallocene catalysts.
  • These monomers include olefins containing functional groups such as ethers, silyl ethers, carbazoles, tertiary phosphines, and tertiary amines.
  • the formed polymers include homopolymers of functionalized monomers as well as copolymers of functionalized monomers with ethylene and alpha-olefins.
  • the formed polymers include both stereoregular (isotactic and syndiotactic) and stereorandom polymers.
  • the functionalized monomers include nonconjugated dienes and alpha-olefins with amine, phosphine, carbazole, and silylether groups.
  • Figures 1A and 1B are C NMR spectra of syndiotactic poly (5-N,N-diisopropyl-1-pentene) and isotactic poly (5-N,N-diisopropyl-1-pentene), respectively.
  • Figure 2 is a C NMR spectrum of 1-hexene/5-
  • N,N-diisopropyl-1-pentene isotactic copolymer N,N-diisopropyl-1-pentene isotactic copolymer.
  • the present invention is based, in part, on the discovery that certain homogeneous Ziegler-Natta catalysts can be used for the polymerization of functionalized alpha-olefins. These catalysts do not require highly Lewis acidic aluminum cocatalysts, in contrast to conventional Ziegler-Natta catalysts.
  • the inventive catalysts comprise cationic Group 4 metallo- cenes in the presence of preferably a "compatible non- coordinating anions.”
  • compatible non- coordinating anions are those as described in EPA Nos. 277 003 and 277 004 filed January 27, 1988 by Turner et al. and EPA No. 427 697-A2 filed October 9, 1990 by Ewen et al.
  • a “compatible non-coordinating anion” means an anion which either does not coordinate with a cation or which is only weakly coordinated to said cation and thereby remaining sufficiently labile to be displaced by a neutral Lewis base.
  • the recitation "compatible non-coordinating anion” specifically refers to an anion which when functioning as a stabilizing anion in the catalyst system of this invention does not transfer an anionic substituent or fragment thereof to said cation thereby forming a neutral four coordinate metallocene and a neutral boron by-product.
  • Compatible anions are those which are not degraded to neutrality when the initially formed complex decomposes.
  • inventive cationic metallocene catalysts are prepared by one of several known procedures as reported in EPA Nos. 277 003 and 277 004 filed January 27, 1988 by Turner et al.; EPA No. 427 697-A2 filed October 9, 1990 by Ewen et al.; Marks et al., J. Am. Chem. Soc. , 113 (1991), p. 3623; Chien et al., J. Am. Chem. Soc , 113 (1991), p. 8570; Bochman et al., Angew. Chem. Intl, Ed. Engl . , 7 (1990), p. 780; and Teuben et al., Organometallics , 11 (1992), p. 362 and references therein, all of which are incoporated herein.
  • the inventive Group 4 metallocenes may be represented by the following formula:
  • Suitable reagents used to generate the active "cationic" metallocene is preferably (but not limited to) one of the following four types: (1) a tertiary ammonium salt R 3 NH + A-, where A is a compatible non-coordinating anion (counterion) as defined by Turner (EPA Nos. 277 003 and 277 004) ; (2) Ox + A- where Ox + is a one electron oxidant and A- is a compatible non-coordinating anion (counterion) as defined by Turner (EPA Nos. 277 003 and 277
  • A- is a compatible non-coordinating anion (counterion) as defined by Turner (EPA Nos. 277 003 and 277 004).
  • the monomers that can be polymerized with the catalyst system include alpha-olefins containing silyl or trityl ethers, trialkyl, dialkylaryl, diarylalkyl or triaryl amines, or trialkyl, dialkylaryl, diarylalkyl or triarylphosphines and alkylcarbazoles.
  • the metallocene component has the general formula (Ln)MX 1 X 2 , which is the same as the Group 4 metal compounds described above.
  • the aluminoxane component is either (i) a linear aluminoxane having the general formula Al 2 OR 4 (Al (R)-O) n or (ii) a cyclic aluminoxane having the general formula (Al (R)-O) n+2 , where n is a number from 4 to 20 and R is a methyl or ethyl radical.
  • the aluminoxane component is generally mixed with a metallocene component in a 100/1 to 10,000/1 molar ratio of aluminum to the Group 4 metal in suitable solvents such as toluene or heptane. It has been demonstrated that the aluminoxane catalysts can polymerize alpha-olefins containing silyether functional groups. (See Examples 12 and 16 herein.)
  • Analytical GPC data were obtained on Waters 10 A, 500 A, and Linear ultrastyragel columns employing a Waters 410 refractive index diffractometer with tetrahydrofuran as the mobil phase; molecular weights were calculated versus polystyrene standards.
  • DSC differential scanning calorimetry
  • TGA thermo gravimetric analysis
  • TMSO trimethylsiloxy
  • TBDMSO tert-butyldimethylsiloxy
  • 4-TMSO-1-pentene, 4-TBDMSO-1- pentene, allyloxytrimethylsilane, allyloxy (tert-butyl- dimethylsilane) were prepared from 1,5-hexadiene-4-ol (Wiley), 4-pentene-1-ol (Wiley) and allylalcohol (Aldrich), respectively, according to literature methods (Chaudhary et al., Tet. Lett . , 2 (1979), p. 99).
  • a 20 ml vial was loaded with 829 mg (1.1 ml, 4.89 mmol) of 5-N,N-diisopropylamino-l- pentene, 2 ml of a Cp 2 Zr(CH 3 ) 2 / toluene solution (8 mg/ml, 0.041 mmol added), and 0.90 ml of toluene.
  • the vial was placed in a toluene bath (20°C) and equipped with a thermometer and stir bar. The reaction was initiated by adding 1.0 ml of a B(C 6 F 5 ) 3 /toluene solution (10.12 mg/ml, 0.020 mmol added).
  • the volatiles were removed in vacuo to leave a yellow oil.
  • a 50 ml schlenk tube was loaded with 12 mg (0.023) of B(C 6 F 5 ) 3 .
  • An addition funnel was loaded with 842 mg (4.97 mmol) of 5-N,N-diisopropylamino-1-pentene, 17 mg of Cp 2 Zr(CH 3 ) 2 and 3.9 ml of toluene and the addition funnel attached to the 50 ml schlenk.
  • the system was sealed, removed from the dry box, and cooled to -78 °C in a dry ice/acetone bath. After approximately 10 minutes, the solution was added to the B(C 6 F 5 ) 3 .
  • the reaction vessel was moved to a dry ice/CCl 4 bath (-25°C).
  • Examples 1-7 are summarized in Table 1 and compared to 1-hexene.
  • Cp* pentamethylcyclopentadienyl
  • EBTHI ethylene-1,2-bis(n 5 -4,5,6,7-tetrahydro-l-indenyl)
  • TMS trimethylsilyl
  • TBDMS tert-butyldimethylsilyl.
  • N,N-diisopropylamino-1-pentene 210 mg (1.06 mmol) of triisobutylaluminum, 5.0 ml of toluene, 20 mg (0.053 mmol) of rac-EBIZrMe 2 , and 14 mg (0.027 mmol) of B(C 6 F 5 ) 3 were reacted at 20°C for 22 hours.
  • GC analysis indicated 48% conversion.
  • the polymer was isolated in the usual manner to obtain 1.59 g of a white, tacky powder which was analyzed by NMR (endgroup analysis indicated M n >25,000).
  • a 20 ml vial was loaded with 832 mg (4.91 mmol) of 5-N,N-diisopropylaminol-pentene, 429 mg (5.10 mmol) of 1-hexene, 3.25 ml of toluene, 68 mg of triisobutylaluminum and stirred for 30 minutes.
  • rac-EBIZrMe 2 (6 mg, 0.016 mmol) and B(C 6 F 5 ) 3 (8 mg, 0.016 mmol) were added.
  • the solution immediately turned dark brown and an exotherm was detected (20-28°C).
  • the reaction was quenched after 65 minutes and worked up in the usual manner to obtain 584 mg (46%) of a colorless, sticky solid.
  • the C NMR spectrum is shown in Fig. 3.
  • the copolymer was treated with a methanol/ HCl solution for 20 minutes and then dried in vacuo. A glassy solid was obtained which was completely soluble in methanol and insoluble in hexanes which indicates that no homopolymer of 1-hexene is present.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
  • Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)

Abstract

Catalyseurs dérivés de la réaction de Cp*2ZrMe2 avec B(B6F5)3 ou [N,N-diméthylanilinium] [B(C6F5)4] (indiqué sous forme de [Cp*ZrMe]+X-, Cp* = pentaméthylcyclopentadiényle, X = B(C¿6?F5)4 ou CH3B(C6F5)3) sont actifs pour l'homopolymérisation de diènes et d'alpha-oléfines fonctionnalisées telles que 4-TMSO-1,6-heptadiène (TMSO = triméthylsiloxy), 5-TBDMSO-1-pentène (TBDMSO = tertbutyldiméthylsiloxy), 5-N,N-diisopropylamino-1-pentène, 5-diphénylphosphino-1-pentène et N-(1-pentène-4-yle)carbazole. D'autres catalyseurs organométalliques tels que [rac (EBTHI)ZrMe]?+X-¿ et [EBIZrMe¿2]?+X- (EBTHI = éthylène-1,2-bis(n5-4,5,6,7-tétrahydro-1-indényle, EBI = éthylène-1,2-bis(1-indényle)) sont des catalyesurs de polymérisation actifs pour la polymérisation d'oléfines fonctionnalisées, bien qu'ils soient plus facilement empoisonnés par les éthers de silyle; les catalyseurs [rac-(EBTHI)ZrMe]+X- polymérisent 4-TBDMSO-1,6-heptadiène et 5-N,N-diisopropylamino-1-pntène. Une série d'autres éthers de silyle ont été polymérisés. Des analyses 13C NMR préliminaires de polymères obtenus à partir des alpha-oléfines fonctionnalisées avec des catalyseurs [(EBTHI)ZrMe]+X- sont compatibles avec des microstructures hautement isotactiques. Des polymères surtout syndiotactiques sont produits à -25° en présence de catalyserus [Cp*¿2?ZrMe]?+X-¿, ce qui est compatible avec le contrôle de fin de chaîne. Le traitement d'éthers de polysilyle avec HCl permet d'obtenir de nouveaux polyalcools. L'ajout de HCl au poly(5-N,N-diisopropylamino-1-pentène) produit le polyélectrolyte correspondant. Les catalyseurs organométalliques/méthylaluminoxane sont actifs pour la polymérisation d'alpha-oléfines contenant des groupes éther de silyle.
PCT/US1993/011186 1992-11-25 1993-11-17 Polymerisation de monomeres fonctionnalises a l'aide de catalyseurs de ziegler-natta WO1994012547A2 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
EP94902289A EP0623149A4 (en) 1992-11-25 1993-11-17 Polymerization of functionalized monomers with ziegler-natta catalysts.
JP6513242A JPH07507095A (ja) 1992-11-25 1993-11-17 チーグラー・ナッタ触媒で官能化した単量体の重合

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US98169692A 1992-11-25 1992-11-25
US07/981,696 1992-11-25

Publications (2)

Publication Number Publication Date
WO1994012547A2 true WO1994012547A2 (fr) 1994-06-09
WO1994012547A3 WO1994012547A3 (fr) 1994-07-21

Family

ID=25528582

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/US1993/011186 WO1994012547A2 (fr) 1992-11-25 1993-11-17 Polymerisation de monomeres fonctionnalises a l'aide de catalyseurs de ziegler-natta

Country Status (4)

Country Link
EP (1) EP0623149A4 (fr)
JP (1) JPH07507095A (fr)
CA (1) CA2128691A1 (fr)
WO (1) WO1994012547A2 (fr)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3357961A (en) * 1965-05-24 1967-12-12 Exxon Research Engineering Co Copolymers of ethylene and hexadiene 1, 5
US4734472A (en) * 1986-12-24 1988-03-29 Exxon Research And Engineering Company Method for preparing functional alpha-olefin polymers and copolymers
US4794096A (en) * 1987-04-03 1988-12-27 Fina Technology, Inc. Hafnium metallocene catalyst for the polymerization of olefins
US4841004A (en) * 1986-11-29 1989-06-20 Hoechst Aktiengesellschaft Process for the preparation of a 1-olefin stereoblock polymer
US4892851A (en) * 1988-07-15 1990-01-09 Fina Technology, Inc. Process and catalyst for producing syndiotactic polyolefins
US4975403A (en) * 1987-09-11 1990-12-04 Fina Technology, Inc. Catalyst systems for producing polyolefins having a broad molecular weight distribution

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3755279A (en) * 1965-06-25 1973-08-28 Exxon Research Engineering Co Copolymerization of alpha olefins with sterically hindered alkenyl amines using ziegler catalysts
GB1094557A (en) * 1965-11-29 1967-12-13 Montedison Spa Polymers of unsaturated tertiary amines

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3357961A (en) * 1965-05-24 1967-12-12 Exxon Research Engineering Co Copolymers of ethylene and hexadiene 1, 5
US4841004A (en) * 1986-11-29 1989-06-20 Hoechst Aktiengesellschaft Process for the preparation of a 1-olefin stereoblock polymer
US4734472A (en) * 1986-12-24 1988-03-29 Exxon Research And Engineering Company Method for preparing functional alpha-olefin polymers and copolymers
US4794096A (en) * 1987-04-03 1988-12-27 Fina Technology, Inc. Hafnium metallocene catalyst for the polymerization of olefins
US4975403A (en) * 1987-09-11 1990-12-04 Fina Technology, Inc. Catalyst systems for producing polyolefins having a broad molecular weight distribution
US4892851A (en) * 1988-07-15 1990-01-09 Fina Technology, Inc. Process and catalyst for producing syndiotactic polyolefins

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
Journal of Applied Polymer Science, Vol. 35, "C-NMR Characterization of Poly (1,5-hexadiene)", pages 825-829 (1988), (CHENG): see page 825, Synopsis; page 827, first paragraph. *
See also references of EP0623149A1 *

Also Published As

Publication number Publication date
WO1994012547A3 (fr) 1994-07-21
EP0623149A1 (fr) 1994-11-09
JPH07507095A (ja) 1995-08-03
CA2128691A1 (fr) 1994-06-09
EP0623149A4 (en) 1995-09-27

Similar Documents

Publication Publication Date Title
US5399635A (en) Process for preparation of monocyclopentadienyl metal complex compounds and method of use
US5387568A (en) Preparation of metallocene catalysts for polymerization of olefins
EP0604908B1 (fr) Procédé de polymérisation d'oléfines alpha utilisant des composés de type métallocène possédant les ligands du type fluorènylique
KR100293264B1 (ko) 폴리올레핀제조용촉매조성물및폴리올레핀의제조방법
US6372930B1 (en) Polymeric ligands, polymeric metallocenes, catalyst systems, preparation, and use
US5714425A (en) Catalyst compositions and process for preparing polyolefins
JP3176609B2 (ja) シンジオタクチック‐ポリオレフィンの製造方法、その方法で使用されるメタロセンおよびこれを含む触媒
JP4829498B2 (ja) ポリオレフィン製造用の触媒および方法
JP2954251B2 (ja) オレフィン重合用触媒
EP0367597B1 (fr) Méthode pour préparer de la cire de polyéthylène par polymérisation en phase gazeuse
JP2669833B2 (ja) オレフインの重合及びオレフインの共重合のための触媒系
KR100291249B1 (ko) 촉매계,올레핀(공)중합을위한이촉매계의용도,촉매계의제조방법과올레핀(공)중합법
WO1999020637A1 (fr) Catalyseurs metallocenes et procedes de preparation et d'utilisation associes
JP2003510430A (ja) 加水分解性オレフィンコポリマー
EP0739361A1 (fr) Constituants de catalyseur pontes par de l'amino siladiyle, et procedes de fabrication et d'utilisation de ces constituants
US6939930B2 (en) Hydrosilane additives for increased polyolefin molecular weight
AU646537B2 (en) Metallocene (CO)polymers, process for their preparation and their use as catalysts
JPH07649B2 (ja) オレフィン重合用触媒成分の製造方法
EP0550075A1 (fr) Utilisation de dérivés à ponts méthylène de complexes dicarbollide cyclopentodiényl de titane, zirconium et hafnium en tant que catalyseurs de polymérisation
KR20050024287A (ko) 용액 상태의 고온 올레핀 중합 방법
CN115956093A (zh) 包含杂化过渡金属化合物的催化剂、使用其制备的烯烃聚合物及它们的制备方法
JP3340064B2 (ja) α−オレフィンの重合及び共重合用の有機金属触媒
CA2284317A1 (fr) Copolymere sequence styrene-butadiene
WO1996027621A1 (fr) Catalyseurs de cyclopentadienyle a plusieurs valences de metaux alcalins du groupe 6b servant a la polymerisation d'alpha-olephines et leur utilisation dans des processus de polymerisation
JP2969152B2 (ja) オレフィンブロック共重合体

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A2

Designated state(s): CA JP

AL Designated countries for regional patents

Kind code of ref document: A2

Designated state(s): AT BE CH DE DK ES FR GB GR IE IT LU MC NL PT SE

AK Designated states

Kind code of ref document: A3

Designated state(s): CA JP

AL Designated countries for regional patents

Kind code of ref document: A3

Designated state(s): AT BE CH DE DK ES FR GB GR IE IT LU MC NL PT SE

WWE Wipo information: entry into national phase

Ref document number: 2128691

Country of ref document: CA

WWE Wipo information: entry into national phase

Ref document number: 1994902289

Country of ref document: EP

121 Ep: the epo has been informed by wipo that ep was designated in this application
WWP Wipo information: published in national office

Ref document number: 1994902289

Country of ref document: EP

WWW Wipo information: withdrawn in national office

Ref document number: 1994902289

Country of ref document: EP