WO2004078795A2 - Group iiib metal complexes with “constrained geometry” fluorenyl based ligands - Google Patents
Group iiib metal complexes with “constrained geometry” fluorenyl based ligands Download PDFInfo
- Publication number
- WO2004078795A2 WO2004078795A2 PCT/EP2004/002378 EP2004002378W WO2004078795A2 WO 2004078795 A2 WO2004078795 A2 WO 2004078795A2 EP 2004002378 W EP2004002378 W EP 2004002378W WO 2004078795 A2 WO2004078795 A2 WO 2004078795A2
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- WO
- WIPO (PCT)
- Prior art keywords
- metallocene catalyst
- catalyst component
- flu
- component according
- thf
- Prior art date
- Legal status (The legal status 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 status listed.)
- Ceased
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/52—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides selected from boron, aluminium, gallium, indium, thallium or rare earths
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07F—ACYCLIC, CARBOCYCLIC OR HETEROCYCLIC COMPOUNDS CONTAINING ELEMENTS OTHER THAN CARBON, HYDROGEN, HALOGEN, OXYGEN, NITROGEN, SULFUR, SELENIUM OR TELLURIUM
- C07F17/00—Metallocenes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F20/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
- C08F20/02—Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
- C08F20/10—Esters
- C08F20/12—Esters of monohydric alcohols or phenols
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/619—Component covered by group C08F4/60 containing a transition metal-carbon bond
Definitions
- the present invention relates to the field of "constrained geometry catalyst” systems based on Group Illb metals of the Periodic Table. It also relates to their synthesis and their use in olefin polymerisation.
- CGC Constrained geometry catalysts
- the present invention aims at preparing catalyst systems efficient in the controlled polymerisation of polar or non polar monomers.
- the present invention discloses a metallocene catalyst component based on a Group Illb metal of the Periodic Table and a bridged constrained geometry fluorenyl-based ligand.
- the present invention discloses a metallocene catalyst component of the general formula [ (Flu-SiR 2 - N- R') M (R") (L) n ] m (I) wherein Flu is a fluorenyl, substituted or unsubstituted, M is a Group Illb metal of the Periodic Table, SiR 2 is a structural bridge between N and Flu (9-position) imparting stereorigidity to the component wherein each R is the same or different and is an alkyl having from 1 to 20 carbon atoms, R' is hydrogen or is of the form ZR $ 3 wherein Z is C or Si and R $ is a hydrocarbyl having from 1 to 20 carbon, R" is hydrogen, or a hydrocarbyl having from 1 to 20 carbon atoms, said hydrocarbyl possibly containing one or more Si atoms, or is a halogen, L is a co-ordinating solvent, n is 0, 1 or 2, and m is 1 or 2.
- the substituents on the fluorenyl are not particularly limited, they can be the same or different and are of the form ZR $ 3 as defined here-above; they include particularly hydrocarbyls having from 1 to 20 carbon atoms. Preferably, they are located at positions 3 and 6, or at positions 4 and 5, or at positions 2 and 7 and more preferably, they are the same.
- M is preferably yttrium, lanthanum or a member of the lanthanide series.
- lanthanide series means the rare earth series of elements having atomic numbers of from 58 to 71.
- M is preferably neodymium, samarium. More preferably, M is yttrium.
- N is substituted and more preferably, the substituent is tert-butyl.
- R" is hydrogen or an alkyl or an aryl or an allyl or a halogen
- m is 1 when R" is an alkyl or an aryl or an allyl
- m is 2 when R" is hydrogen or a halogen.
- R" is a halogen, it is preferably Cl, I, or Br.
- the co-ordinating solvent is typically an ether such as for example tetrahydrofuran (THF), dimethoxyether (DME) or diethyl oxide (Et 2 O).
- ether such as for example tetrahydrofuran (THF), dimethoxyether (DME) or diethyl oxide (Et 2 O).
- compounds of type (I), wherein R" is a halogen must be alkylated first with an adequate reagent.
- Typical reagents can be selected from LiR * , R * MgX, Mg R * 2 , Al R * 3 , Al R * nXa-n, [Li] + [AIR * n X 3-n ]- and methylalumoxane (MAO), wherein R * is an alkyl, aryl or allyl having from 1 to 20 carbon atoms and X is a halogen, preferably Cl. This list should not be considered as limitative.
- the present invention discloses a metallocene catalyst component of the general formula
- Q is an alkali, an earth alkali or a Group Ilia metal of the Periodic Table and p is from 2 to 4.
- Q is preferably Li, Na, Mg or Al.
- p When the ion-pair in complex II is fully dissociated, p is 4 and when the ion-pair is partially associated, p is 2 or 3.
- the present invention discloses a first method, based on a salt metathesis reaction method for preparing the catalyst components (I) or (II) that comprises the steps of: a) suspending MX 3 (THF) n in an ether; b) suspending a deprotonated dilithium salt [Flu-SiR 2 - N- R']Li 2 in the same or another ether; c) carrying out the salt metathesis reaction of suspensions a) and b) at a temperature of from -80 °C to 60 °C.
- complex (I) wherein R" is a halogen can comprise the additional step of alkylation with an alkylating agent to give complex (I) wherein R" is a hydrocarbyl as defined above.
- Suitable alkylating agent can be selected from LiR + , R + MgX, MgR + 2 , AIR + 3 , AIR + n X 3 - n and [Li] + [AIR + n X3-n] " wherein R + is an alkyl, an aryl or an allyl having from 1 to 20 carbon atoms and X is a halogen, preferably Cl.
- the present invention discloses a second method, based on an alkane elimination reaction, for preparing specifically the catalyst component
- R" is specifically a hydrocarbyl having from 1 to 20 carbon atoms, said hydrocarbyl possibly containing one or more Si atoms, that comprises the steps of reacting the triscarbyl complex M(R") 3 (L) n , either presynthesised or generated in situ, with one equivalent of the diproteo ligand (FluH-SiR 2 - NH- R').
- the triscarbyl complex M(R")3(L) n is preferably generated in situ as the reaction product of MCI 3 (THF) n and 3 equivalents of LiR".
- the reaction temperature for the preparation of complex (I) is of from 0 °C up to 75 °C and preferably of from 40 to 50 °C.
- M is preferably Yttrium and the bridge SiR 2 , is preferably a dialkyl silyl.
- Suitable hydrogenolising agents can be selected from dihydrogen or an hydrosilane, e.g. phenylsilane.
- the reaction is preferably carried out at room temperature at about 25 °C and at atmospheric pressure in an hydrocarbon solvent, e.g. benzene or toluene.
- the reaction product is insoluble in both polar (ethers) and non-polar (hydrocarbons) solvents.
- the present invention further discloses a catalyst system based upon any one or more of catalyst components of formulas (I) and/or (II) and a suitable activating agent and/or a transfer agent.
- the present invention discloses a process for polymerisation comprising the steps of: a) introducing a catalyst system based on any one or more of catalyst components of formulas (I) and/or (II) in the reactor, b) optionally introducing an activating agent or a transfer agent in the reactor, c) feeding a monomer and an optional comonomer, d) maintaining the system under polymerisation conditions, e) retrieving the desired polymer.
- the optional activating agent includes Lewis acids having an ionising action and having a low or no co-ordinating capability.
- all the activators used with the metals Group IV of the Periodic Table can be used in the present invention.
- Suitable aluminium-containing activating agents comprise an alumoxane an aluminium alkyl or an alkylaluminate [Li] + [AIR * n X 3 . n ] "
- alumoxanes that can be used in the present invention are well known and preferably comprise oligomeric linear and/or cyclic alkyl alumoxanes represented by the formula (III):
- alumoxanes from, for example, aluminium trimethyl and water, a mixture of linear and cyclic compounds is obtained.
- Suitable boron-containing activating agents may comprise a triphenylcarbenium boronate, such as tetrakis-pentafluorophenyl-borato-triphenylcarbenium as described in EP-A-0427696:
- activating agents include hydroxy isobutylaluminium and a metal aluminoxinate.
- the transfer agents comprise for example H 2 and hydrosilanes of the formula HSiR'" 3 wherein each R"' is the same or different and is either an H atom or a hydrocarbyl having from 1 to 20 carbon atoms. They are selected in accordance with the monomer to be polymerised.
- the monomers that can be used in the present invention include non polar monomers such as for example ethylene, alpha-olefins, styrene and polar monomers such as for example (meth)acrylates or dienes.
- non polar monomers such as for example ethylene, alpha-olefins, styrene and polar monomers such as for example (meth)acrylates or dienes.
- styrene and methyl methacrylate have been used.
- the catalyst system of the present invention may be employed in any type of homo- or co-polymerisation method, provided that the required catalytic activity is not impaired.
- the catalyst system is employed in a bulk polymerisation process or in a solution polymerisation process, which is homogeneous, or in a slurry process, which is heterogeneous.
- typical solvents include THF or hydrocarbons having from 4 to 7 carbon atoms such as heptane, toluene or cyclohexane.
- the catalyst system In a slurry process, it is necessary to immobilise the catalyst system on an inert support, particularly a porous solid support such as talc, inorganic oxides and resinous support materials such as polyolefin.
- an inert support particularly a porous solid support such as talc, inorganic oxides and resinous support materials such as polyolefin.
- the support material is an inorganic oxide in its finely divided form.
- Suitable inorganic oxide materials that are desirably employed in accordance with this invention include group IIA, IIIA, IVA, or IVB metal oxides such as silica, alumina and mixtures thereof.
- Other suitable support materials can be employed, for example, finely divided functionalised polyolefins such as finely divided polyethylene.
- the support is a silica support having a surface area of from 200- 700 m 2 /g and a pore volume of from 0.5-3 ml/g.
- the polymerisation temperatures range from -20 °C up to 100 °C.
- the present invention also covers the polymers obtainable by polymerisation in the presence of the catalysts components described hereabove.
- Figure 1 represents the crystal structure of the molecule [S. ⁇ -di-'Bu-CiaHe- SiMe 2 -N t Bu]Y(CH 2 SiMe 3 )(THF) 2 (1).
- Figure 2 represents the 1 H NMR spectrum of complex[3,6-di- t Bu-Ci3H6-SiMe 2 - N t Bu]Y(CH 2 SiMe 3 )CT ' HF)2 (1) in C 6 D 6 at 25 °C.
- Figure 3 represents the 13 C NMR spectrum of complex ([3,6-di- t Bu-C ⁇ 3 H 6 -SiMe 2 -
- Figure 4 represents the 1 H NMR spectrum of complex [3,6-di- t Bu-C ⁇ 3 H 6 -SiMe 2 - N t Bu]Y(CH 2 SiMe 3 )(THF) 2 (1) in C 6 D 6 at -70 °C.
- Figure 5 represents the 1 H NMR spectrum of complex [ ⁇ ( t Bu 2 -C 13 H 6 )-SiMe 2 - N l Bu ⁇ 2 Yr[Li(THF) 4 ] + (2) in THF-d 8 at 25 °C.
- Figure 6 represents the 13 C NMR spectrum of complex [ ⁇ ( t BurC ⁇ 3 H ⁇ )-SiMe 2 - NteufeY ⁇ LiO ⁇ FM * ( 2 ) in THF-ds at 25 °C.
- Figure 7 represents the crystal structure of the molecule ' SiMe 2 -N t Bu ⁇ 2 Lar[Li(OEl2)2] + (4)
- Figure 8 represents the crystal structure of the molecule [(S. ⁇ -di-'Bu-CiaHe- SiMe 2 -N t Bu)Nd( ⁇ -CI)(THF)] 2 (5).
- the 1 H NMR spectrum of complex (1) (benzene-cfe, 200 MHz, -70 °C) is represented in Figure 3. The NMR spectroscopy thus indicates that on the NMR time scale, complex (1) is symmetric in benzene at 25 °C, but appears dissymmetric at a temperature lower than -30 °C.
- THF THF
- molecule (1) can be considered formally as a 14-electron complex and coordination number of the yttrium atom is 6. Both coordinated THF ligands are not equivalent according to X-ray data; the difference between the two Y-O distances is 0.05 A, suggesting that one THF molecule could be involved in dissociative processes.
- Method B A solution of [C ⁇ 3 H 8 -SiMe 2 - NtBu]Y(CH 2 TMS)(THF) 2 (0.125 g, 0.172 mmol) in benzene (5 mL) was exposed in hydrogene atmosphere (1 atm, 25 °C) for 12 hours to yield after similar workup 30 mg of a pale-yellow insoluble product.
- MMA methyl methacrylate
- styrene polymerisation of methyl methacrylate (MMA) and styrene have been carried out with complexes (1), (2) and (6).
- Complexes (1) and (2) were prepared as disclosed here-above.
- Complex (6) is an Y-hydride complex.
- Complex (2) reacts smoothly with bulk MMA at room temperature and 50 °C to give atactic PMMA of narrow molecular weight distribution (MWD).
- the molecular weight distribution is defined by the polydispersion index D that is the ratio Mw/Mn of the weight average molecular weight Mw over the number average molecular weight Mn.
- Alkyl complex (1) initiates sluggishly polymerization of MMA and styrene. The polymerization results are displayed in Table I.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
- Polymerization Catalysts (AREA)
Abstract
Description
Claims
Priority Applications (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| KR1020057016497A KR101157702B1 (en) | 2003-03-07 | 2004-03-04 | Group b metal complexes with constrained geometry fluorenyl based ligands |
| ES04717105.3T ES2520865T3 (en) | 2003-03-07 | 2004-03-04 | Group IIIb metal complexes with fluorenyl-based ligands with restricted geometry |
| EP04717105.3A EP1601702B1 (en) | 2003-03-07 | 2004-03-04 | Group iiib metal complexes with 'constrained geometry' fluorenyl based ligands |
| US10/548,506 US7388062B2 (en) | 2003-03-07 | 2004-03-04 | Group IIIb metal complexes with “constrained geometry” fluorenyl based ligands |
| JP2006504593A JP5032112B2 (en) | 2003-03-07 | 2004-03-04 | Group IIIB metal complexes with "constrained geometry" ligands based on fluorenyl |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR0302832A FR2852015B1 (en) | 2003-03-07 | 2003-03-07 | STRESSED GEOMETRY CATALYST COMPONENTS COMPRISING A FLUORENYL LIGANT AND BASED ON GROUP IIIB METALS |
| FR03/02832 | 2003-03-07 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2004078795A2 true WO2004078795A2 (en) | 2004-09-16 |
| WO2004078795A3 WO2004078795A3 (en) | 2004-12-02 |
Family
ID=32865325
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/EP2004/002378 Ceased WO2004078795A2 (en) | 2003-03-07 | 2004-03-04 | Group iiib metal complexes with “constrained geometry” fluorenyl based ligands |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US7388062B2 (en) |
| EP (1) | EP1601702B1 (en) |
| JP (2) | JP5032112B2 (en) |
| KR (1) | KR101157702B1 (en) |
| CN (1) | CN1756772A (en) |
| ES (1) | ES2520865T3 (en) |
| FR (1) | FR2852015B1 (en) |
| WO (1) | WO2004078795A2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016196293A1 (en) * | 2015-05-29 | 2016-12-08 | Dow Global Technologies Llc | A process for producing a polyolefin |
| US11041027B2 (en) | 2015-06-30 | 2021-06-22 | Dow Global Technologies Llc | Polymerization process for producing ethylene based polymers |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4923553B2 (en) * | 2005-12-15 | 2012-04-25 | 宇部興産株式会社 | Process for producing conjugated diene polymer |
| JP2008255341A (en) * | 2007-03-09 | 2008-10-23 | Nippon Zeon Co Ltd | Method for producing cyclic olefin addition polymer, catalyst for cyclic olefin addition polymerization, and transition metal compound |
| CN109796954B (en) * | 2019-01-08 | 2021-07-06 | 中国石油化工股份有限公司 | Temperature-resistant salt-resistant water-soluble multi-component copolymer and preparation method and application thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0277004A1 (en) | 1987-01-30 | 1988-08-03 | Exxon Chemical Patents Inc. | Catalysts, method of preparing these catalysts and method of using said catalysts |
| EP0427696A2 (en) | 1989-10-10 | 1991-05-15 | Fina Technology, Inc. | Process and catalyst for producing syndiotactic polymers |
| EP0980873A2 (en) | 1998-08-14 | 2000-02-23 | Basf Aktiengesellschaft | Binuclear metal hydride complexes and their use as catalysts for the (co)polymerization of polar monomers |
| WO2001042314A1 (en) | 1999-12-09 | 2001-06-14 | Basf Aktiengesellschaft | Method for (co)polymerizing polar and non-polar monomers |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5436305A (en) * | 1991-05-09 | 1995-07-25 | Phillips Petroleum Company | Organometallic fluorenyl compounds, preparation, and use |
| US5464906A (en) * | 1994-11-21 | 1995-11-07 | The Dow Chemical Company | Ethylene homopolymerization using group 3 metal complexes |
| MXPA03003389A (en) * | 2000-10-19 | 2004-01-26 | Exxonmobil Chem Patents Inc | Cationic group-3 catalyst system. |
-
2003
- 2003-03-07 FR FR0302832A patent/FR2852015B1/en not_active Expired - Fee Related
-
2004
- 2004-03-04 WO PCT/EP2004/002378 patent/WO2004078795A2/en not_active Ceased
- 2004-03-04 KR KR1020057016497A patent/KR101157702B1/en not_active Expired - Fee Related
- 2004-03-04 CN CNA2004800058257A patent/CN1756772A/en active Pending
- 2004-03-04 EP EP04717105.3A patent/EP1601702B1/en not_active Expired - Lifetime
- 2004-03-04 US US10/548,506 patent/US7388062B2/en not_active Expired - Fee Related
- 2004-03-04 ES ES04717105.3T patent/ES2520865T3/en not_active Expired - Lifetime
- 2004-03-04 JP JP2006504593A patent/JP5032112B2/en not_active Expired - Fee Related
-
2011
- 2011-08-18 JP JP2011178891A patent/JP5936318B2/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0277004A1 (en) | 1987-01-30 | 1988-08-03 | Exxon Chemical Patents Inc. | Catalysts, method of preparing these catalysts and method of using said catalysts |
| EP0427696A2 (en) | 1989-10-10 | 1991-05-15 | Fina Technology, Inc. | Process and catalyst for producing syndiotactic polymers |
| EP0980873A2 (en) | 1998-08-14 | 2000-02-23 | Basf Aktiengesellschaft | Binuclear metal hydride complexes and their use as catalysts for the (co)polymerization of polar monomers |
| WO2001042314A1 (en) | 1999-12-09 | 2001-06-14 | Basf Aktiengesellschaft | Method for (co)polymerizing polar and non-polar monomers |
Non-Patent Citations (5)
| Title |
|---|
| K. C. HULTZSCH; P. VOTH; K. BECKERLE; T. P. SPANIOL; J. OKUDA, ORGANOMETALLICS, vol. 19, 2000, pages 228 |
| P. J. SHAPIRO; W. D. COTTER; W. P. SCHAEFER; J. A. LABINGER; J. E. BERCAW, J. AM. CHEM. SOC., vol. 116, 1994, pages 4623 |
| S. ARNDT; J. OKUDA, CHEM. REV., vol. 102, 2002, pages 1953 |
| S. TIAN; V. M. ARREDONDO; C. L. STERN; T. J. MARKS, ORGANOMETALLICS, vol. 18, 1999, pages 2568 |
| Y. MU; W. PIERS; M.-A. MACDONALD; M. J. ZAWOROTKO, CAN. J. CHEM., vol. 73, 1995, pages 2233 |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2016196293A1 (en) * | 2015-05-29 | 2016-12-08 | Dow Global Technologies Llc | A process for producing a polyolefin |
| US10465020B2 (en) | 2015-05-29 | 2019-11-05 | Dow Global Technologies Llc | Process for producing a polyolefin |
| US11041027B2 (en) | 2015-06-30 | 2021-06-22 | Dow Global Technologies Llc | Polymerization process for producing ethylene based polymers |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2004078795A3 (en) | 2004-12-02 |
| KR20050118274A (en) | 2005-12-16 |
| JP5936318B2 (en) | 2016-06-22 |
| KR101157702B1 (en) | 2012-06-20 |
| US7388062B2 (en) | 2008-06-17 |
| ES2520865T3 (en) | 2014-11-11 |
| US20060264586A1 (en) | 2006-11-23 |
| EP1601702B1 (en) | 2014-08-06 |
| JP2006519902A (en) | 2006-08-31 |
| JP2011252165A (en) | 2011-12-15 |
| FR2852015B1 (en) | 2007-06-22 |
| CN1756772A (en) | 2006-04-05 |
| EP1601702A2 (en) | 2005-12-07 |
| FR2852015A1 (en) | 2004-09-10 |
| JP5032112B2 (en) | 2012-09-26 |
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