WO2014208852A1 - 이핵 메탈로센 화합물, 및 이의 제조방법 - Google Patents
이핵 메탈로센 화합물, 및 이의 제조방법 Download PDFInfo
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- WO2014208852A1 WO2014208852A1 PCT/KR2013/012320 KR2013012320W WO2014208852A1 WO 2014208852 A1 WO2014208852 A1 WO 2014208852A1 KR 2013012320 W KR2013012320 W KR 2013012320W WO 2014208852 A1 WO2014208852 A1 WO 2014208852A1
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- Prior art keywords
- carbon atoms
- radicals
- alkyl
- aryl
- halogen
- Prior art date
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- 150000001875 compounds Chemical class 0.000 title claims abstract description 73
- 238000000034 method Methods 0.000 title claims abstract description 20
- -1 Halogen radicals Chemical class 0.000 claims description 113
- 125000004432 carbon atom Chemical group C* 0.000 claims description 110
- 125000003118 aryl group Chemical group 0.000 claims description 31
- 125000001931 aliphatic group Chemical group 0.000 claims description 23
- 239000000126 substance Substances 0.000 claims description 23
- 229910052736 halogen Inorganic materials 0.000 claims description 22
- 150000005840 aryl radicals Chemical class 0.000 claims description 20
- 125000001424 substituent group Chemical group 0.000 claims description 17
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 14
- BZLVMXJERCGZMT-UHFFFAOYSA-N Methyl tert-butyl ether Chemical compound COC(C)(C)C BZLVMXJERCGZMT-UHFFFAOYSA-N 0.000 claims description 13
- 125000000217 alkyl group Chemical group 0.000 claims description 12
- 239000001257 hydrogen Substances 0.000 claims description 12
- 229910052739 hydrogen Inorganic materials 0.000 claims description 12
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 10
- 239000010936 titanium Substances 0.000 claims description 10
- 150000002367 halogens Chemical class 0.000 claims description 7
- 229910052751 metal Inorganic materials 0.000 claims description 7
- 239000002184 metal Substances 0.000 claims description 7
- 229910052757 nitrogen Inorganic materials 0.000 claims description 7
- 229910052719 titanium Inorganic materials 0.000 claims description 6
- 229910052723 transition metal Inorganic materials 0.000 claims description 6
- 150000003624 transition metals Chemical class 0.000 claims description 6
- 238000003756 stirring Methods 0.000 claims description 5
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical group [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 3
- MDFFNEOEWAXZRQ-UHFFFAOYSA-N aminyl Chemical compound [NH2] MDFFNEOEWAXZRQ-UHFFFAOYSA-N 0.000 claims description 3
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- VSZWPYCFIRKVQL-UHFFFAOYSA-N selanylidenegallium;selenium Chemical compound [Se].[Se]=[Ga].[Se]=[Ga] VSZWPYCFIRKVQL-UHFFFAOYSA-N 0.000 claims description 3
- 229910052735 hafnium Inorganic materials 0.000 claims description 2
- VBJZVLUMGGDVMO-UHFFFAOYSA-N hafnium atom Chemical compound [Hf] VBJZVLUMGGDVMO-UHFFFAOYSA-N 0.000 claims description 2
- 150000002431 hydrogen Chemical class 0.000 claims description 2
- 239000003054 catalyst Substances 0.000 abstract description 25
- 230000000694 effects Effects 0.000 abstract description 13
- 229920000098 polyolefin Polymers 0.000 abstract description 11
- 239000000758 substrate Substances 0.000 abstract description 5
- 230000001747 exhibiting effect Effects 0.000 abstract 1
- 229920001577 copolymer Polymers 0.000 description 16
- 239000012968 metallocene catalyst Substances 0.000 description 13
- 229920000642 polymer Polymers 0.000 description 10
- 239000002904 solvent Substances 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 9
- 238000002474 experimental method Methods 0.000 description 9
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 8
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 7
- 239000005977 Ethylene Substances 0.000 description 7
- 230000000704 physical effect Effects 0.000 description 7
- 238000009826 distribution Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 239000000203 mixture Substances 0.000 description 5
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000010924 continuous production Methods 0.000 description 4
- 238000007334 copolymerization reaction Methods 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- LWNGJAHMBMVCJR-UHFFFAOYSA-N (2,3,4,5,6-pentafluorophenoxy)boronic acid Chemical compound OB(O)OC1=C(F)C(F)=C(F)C(F)=C1F LWNGJAHMBMVCJR-UHFFFAOYSA-N 0.000 description 3
- JLTDJTHDQAWBAV-UHFFFAOYSA-N N,N-dimethylaniline Chemical compound CN(C)C1=CC=CC=C1 JLTDJTHDQAWBAV-UHFFFAOYSA-N 0.000 description 3
- 230000008859 change Effects 0.000 description 3
- 150000007523 nucleic acids Chemical class 0.000 description 3
- 102000039446 nucleic acids Human genes 0.000 description 3
- 108020004707 nucleic acids Proteins 0.000 description 3
- NFHFRUOZVGFOOS-UHFFFAOYSA-N palladium;triphenylphosphane Chemical compound [Pd].C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1.C1=CC=CC=C1P(C=1C=CC=CC=1)C1=CC=CC=C1 NFHFRUOZVGFOOS-UHFFFAOYSA-N 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- SMWDFEZZVXVKRB-UHFFFAOYSA-N Quinoline Chemical compound N1=CC=CC2=CC=CC=C21 SMWDFEZZVXVKRB-UHFFFAOYSA-N 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 239000011954 Ziegler–Natta catalyst Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- WERYXYBDKMZEQL-UHFFFAOYSA-N butane-1,4-diol Chemical compound OCCCCO WERYXYBDKMZEQL-UHFFFAOYSA-N 0.000 description 2
- 230000014509 gene expression Effects 0.000 description 2
- 230000003993 interaction Effects 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000001603 reducing effect Effects 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 240000002319 Citrus sinensis Species 0.000 description 1
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- 239000012190 activator Substances 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 125000005530 alkylenedioxy group Chemical group 0.000 description 1
- 125000003368 amide group Chemical group 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 230000002902 bimodal effect Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000010960 commercial process Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 125000000058 cyclopentadienyl group Chemical group C1(=CC=CC1)* 0.000 description 1
- 230000000593 degrading effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- ZSWFCLXCOIISFI-UHFFFAOYSA-N endo-cyclopentadiene Natural products C1C=CC=C1 ZSWFCLXCOIISFI-UHFFFAOYSA-N 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- XXMIOPMDWAUFGU-UHFFFAOYSA-N hexane-1,6-diol Chemical compound OCCCCCCO XXMIOPMDWAUFGU-UHFFFAOYSA-N 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- LPAGFVYQRIESJQ-UHFFFAOYSA-N indoline Chemical compound C1=CC=C2NCCC2=C1 LPAGFVYQRIESJQ-UHFFFAOYSA-N 0.000 description 1
- 239000003446 ligand Substances 0.000 description 1
- 125000005647 linker group Chemical group 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000003960 organic solvent Substances 0.000 description 1
- 125000002524 organometallic group Chemical group 0.000 description 1
- 125000000843 phenylene group Chemical group C1(=C(C=CC=C1)*)* 0.000 description 1
- 239000002685 polymerization catalyst Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 150000003254 radicals Chemical class 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
- 238000010561 standard procedure Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- 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
- C07F7/00—Compounds containing elements of Groups 4 or 14 of the Periodic Table
- C07F7/28—Titanium compounds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D401/00—Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, at least one ring being a six-membered ring with only one nitrogen atom
- C07D401/02—Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, at least one ring being a six-membered ring with only one nitrogen atom containing two hetero rings
- C07D401/10—Heterocyclic compounds containing two or more hetero rings, having nitrogen atoms as the only ring hetero atoms, at least one ring being a six-membered ring with only one nitrogen atom containing two hetero rings linked by a carbon chain containing aromatic rings
-
- 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
- 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
- C08F4/72—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44
- C08F4/74—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44 selected from refractory metals
- C08F4/76—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from metals not provided for in group C08F4/44 selected from refractory metals selected from titanium, zirconium, hafnium, vanadium, niobium or tantalum
Definitions
- the present invention relates to a dinuclear metallocene compound and a method for producing the same. More specifically, the present invention relates to a dinuclear metallocene compound having a novel structure capable of producing a high molecular weight polyolefin, and a method for producing the same.
- the Ziegler-Natta catalyst which is widely applied to existing commercial processes, is characterized by a wide molecular weight distribution of the produced polymer because it is a multi-site catalyst, and the composition of the comonomer is not uniform, thereby limiting the desired physical properties.
- Metallocene catalysts are dense active site catalysts with only one type of active site, and have a narrow molecular weight distribution of the resulting polymers, and have a wide range of molecular weight, stereoregularity, crystallization, and especially comonomers depending on the structure of the catalyst and ligand. There is an advantage that can be adjusted.
- polyolefins polymerized with a metallocene catalyst have a narrow molecular weight distribution, and thus, when used in some products, there is a problem in that the application of the polyolefins in the field is difficult due to the extruded load. I've been trying a lot.
- US Pat. No. 15,032,562 describes a process for preparing a polymerization catalyst by supporting two different transition metal catalysts on one supported catalyst. It is a method of producing a bimodal distribution polymer by supporting a titanium (Ti) -based Ziegler-Natta catalyst generating high molecular weight and a zirconium (Zr) -based metallocene catalyst generating low molecular weight on one support.
- Ti titanium
- Zr zirconium
- Korean Patent Application No. 2003-12308 discloses a method of controlling molecular weight distribution by supporting a dual-nuclear metallocene catalyst and a mononuclear metallocene catalyst on a carrier together with an activator to polymerize by changing the combination of catalysts in the reactor. Is starting. However, this method is limited in realizing the characteristics of each catalyst at the same time, and also has the disadvantage that the metallocene catalyst portion is released from the carrier component of the finished catalyst to cause fouling in the reactor. In addition, a synthesis method of a Group 4 metal metallocene catalyst having a biphenylene bridge and polymerization of ethylene and styrene using the catalyst have been reported (Organometallics, 2005, 24, 3618).
- the activity of the catalyst is higher than that of the mononuclear metallocene catalyst and the molecular weight of the obtained polymer is described.
- Another method has been reported that the bridge structure of the Group 4 heteronuclear metallocene catalyst can be changed to change the reaction properties of the catalyst (Eur. Polym, J. 2007, 43, 1436).
- an object of the present invention is to provide a dinuclear metallocene compound of a novel structure capable of producing a high molecular weight polyolefin with high activity.
- R1 to R4 may be the same as or different from each other, and each independently hydrogen; Halogen radicals; Alkyl radicals having 1 to 20 carbon atoms; Alkenyl radicals having 2 to 20 carbon atoms; Silyl radicals; Aryl radicals having 6 to 20 carbon atoms; Alkylaryl radicals having 7 to 20 carbon atoms; Or an arylalkyl radical having 7 to 20 carbon atoms; Two or more adjacent ones of R1 to R4 may be connected to each other to form an aliphatic ring, an 'or an aromatic ring;
- R5 to R7 may be the same as or different from each other, and each independently hydrogen; Halogen radicals; Alkyl radicals having 1 to 20 carbon atoms; Alkenyl radicals having 2 to 20 carbon atoms; Aryl radicals having 6 to 20 carbon atoms; Alkylaryl radicals having 7 to 20 carbon atoms; Arylalkyl radicals having 7 to 20 carbon atoms; Alkoxy radicals having 1 to 20 carbon atoms; Aryloxy radicals having 6 to 20 carbon atoms; Or amido radicals; R5 to above. Two or more adjacent to R 7 may be linked to each other to form an aliphatic ring or an aromatic ring;
- CY is an aliphatic or aromatic ring containing nitrogen, halogen, carbon number
- ⁇ is a Group 4 transition metal
- XI is a halogen radical
- Alkyl radicals having 1 to 20 carbon atoms Alkenyl radicals having 2 to 20 carbon atoms
- Aryl radicals having 6 to 20 carbon atoms Malkyaryl radicals having 7 to 20 carbon atoms; Arylalkyl radicals having 7 to 20 carbon atoms; Alkyl amido radicals having 1 to 20 carbon atoms; Aryl amido radicals having 6 to 20 carbon atoms; Or an alkylidene radical of 1 to 20 carbon atoms;
- n is an integer of 0-10.
- a second aspect of the present invention provides a method for preparing the dinuclear metallocene compound.
- the dinuclear metallocene compound according to the present invention is a dinuclear metallocene compound having a novel structure, and unlike a single active site catalyst, it is possible to provide a catalyst having multiple active sites showing high activity due to high accessibility with a substrate.
- the catalyst of the present invention can produce a high molecular weight polyolefin.
- first and second are used to describe various components, which terms are used only for the purpose of distinguishing one component from other components.
- each layer or element when each layer or element is referred to as being formed “on” or “on” of each layer or element, it means that each layer or element is directly formed on each layer or element, or the other That a layer or element may additionally be formed between each layer and on the object, substrate it means.
- the present invention provides a dinuclear metallocene compound represented by the following Chemical Formula 1.
- R1 to R4 may be the same as or different from each other, and each independently hydrogen; Halogen radicals; Alkyl radicals having 1 to 20 carbon atoms; Alkenyl radicals having 2 to 20 carbon atoms; Silyl radicals; Aryl radicals having 6 to 20 carbon atoms; Alkylaryl radicals having 7 to 20 carbon atoms; Or an arylalkyl radical having 7 to 20 carbon atoms; Two or more adjacent ones of R1 to R4 may be connected to each other to form an aliphatic ring or an aromatic ring;
- R5 to R7 may be the same as or different from each other, and each independently hydrogen; Halogen radicals; Alkyl radicals having 1 to 20 carbon atoms; Alkenyl radicals having 2 to 20 carbon atoms; Aryl radicals having 6 to 20 carbon atoms; Alkylaryl radicals having 7 to 20 carbon atoms; Arylalkyl radicals having 20 to 20 carbon atoms; Alkoxy radicals having 1 to 20 carbon atoms; Aryloxy radicals having 6 to 20 carbon atoms; Or amido Radical; Two or more adjacent ones of R5 to R7 may be connected to each other to form an aliphatic ring or an aromatic ring;
- CY is an aliphatic or aromatic ring containing nitrogen, halogen, carbon number
- M is a Group 4 transition metal
- XI is a halogen radical; Alkyl radicals having 1 to 20 carbon atoms; Alkenyl radicals having 2 to 20 carbon atoms; Aryl radicals having 6 to 20 carbon atoms; Alkylaryl radicals having 7 to 20 carbon atoms; Arylalkyl radicals having 7 to 20 carbon atoms; Alkyl amido radicals having 1 to 20 carbon atoms; Aryl amido radicals having 6 to 20 carbon atoms; Or an alkylidene radical of 1 to 20 carbon atoms;
- n is an integer of 0-10.
- R 1 to R 7 are each independently hydrogen, an alkyl group having 1 to 20 carbon atoms, an aryl group having 6 to 20 carbon atoms, or the R 1 to R 7 Two adjacent to each other may be connected to each other to form one or more aliphatic rings or aromatic rings, but the present invention is not limited thereto.
- the CY may be a pentagonal or hexagonal aliphatic or aromatic ring including nitrogen unsubstituted or substituted with an alkyl group having 1 to 20 carbon atoms, but the present invention is not limited thereto.
- M may be titanium (Ti), zirconium (Zr), or hafnium (Hf), and XI may be a halogen or an alkyl group having 1 to 20 carbon atoms, but the present invention is not limited thereto.
- Examples of the dinuclear metallocene compound represented by Formula 1 include the following compounds, but are not limited thereto.
- the present invention provides a method for producing a dinuclear metallocene compound represented by the following Chemical Formula 1, comprising the step of reacting a compound represented by the following Chemical Formula 2 and a compound represented by the following Chemical Formula 3; to provide.
- R1 to R4 may be the same as or different from each other, and each independently hydrogen; Halogen radicals; Alkyl radicals having 1 to 20 carbon atoms; Alkenyl radicals having 2 to 20 carbon atoms; Silyl radicals; Aryl radicals having 6 to 20 carbon atoms; Alkylaryl radicals having 7 to 20 carbon atoms; Or an arylalkyl radical having 7 to 20 carbon atoms; Two or more adjacent ones of R1 to R4 may be connected to each other to form an aliphatic ring or an aromatic ring;
- R5 to R7 may be the same as or different from each other, and each independently hydrogen; Halogen radicals; Alkyl radicals having 1 to 20 carbon atoms; Alkenyl radicals having 2 to 20 carbon atoms; Aryl radicals having 6 to 20 carbon atoms; Alkylaryl radicals having 7 to 20 carbon atoms; Arylalkyl radicals having 7 to 20 carbon atoms; Alkoxy radicals having 1 to 20 carbon atoms; Aryloxy radicals having 6 to 20 carbon atoms; Or amido Radical; Two or more adjacent ones of R5 to R7 may be connected to each other to form an aliphatic ring or an aromatic ring;
- CY is an aliphatic or aromatic ring containing nitrogen, and may be substituted or unsubstituted with halogen, alkyl having 1 to 20 carbon atoms or aryl radicals, and when there are a plurality of substituents, two or more substituents of the substituents may be linked to each other. May form an aliphatic or aromatic ring;
- M is a Group 4 transition metal
- XI and X2 may be the same as or different from each other, and each independently a halogen radical; Alkyl radicals having 1 to 20 carbon atoms; Alkenyl radicals having 2 to 20 carbon atoms; Aryl radicals having 6 to 20 carbon atoms; Alkylaryl radicals having 7 to 20 carbon atoms; Arylalkyl radicals having 7 to 20 carbon atoms; Alkyl amido radicals having 1 to 20 carbon atoms; Aryl amido radicals having 6 to 20 carbon atoms; Or an alkylidene radical of 1 to 20 carbon atoms;
- n is an integer of 0-10.
- the method for preparing a dinuclear metallocene compound of the present invention may be performed by mixing a mononuclear metallocene compound represented by Formula 2 and a diol compound represented by Formula 3 and then stirring the mixture for a predetermined time.
- the stirring temperature is about -30 to about 25 ° C, preferably at room temperature, the stirring time may be carried out by stirring for at least 12 hours, for example about 12 hours to about 36 hours, but the present invention is not limited thereto. .
- the agitation may be performed in an organic solvent such as methyl tertiary-butyl ether (MTBE) or toluene, and may be obtained in the form of a dinuclear metallocene compound by extraction in n-Hexane, but the preparation method of the present invention is not limited thereto. Do not.
- an organic solvent such as methyl tertiary-butyl ether (MTBE) or toluene
- the diol compound represented by Chemical Formula 3 may be reacted with 5 equivalents to the mononuclear metallocene compound represented by Chemical Formula 2 ⁇
- the method for preparing a mononuclear metallocene compound represented by Chemical Formula 1 is The present invention may be prepared according to methods known in the art, and is not particularly limited.
- a binuclear metallocene compound represented by Chemical Formula 1 may be prepared by a simple process under relatively mild conditions, and by controlling the distance of the nucleus active site according to the alkyl chain length of the diol compound, Activity can be easily controlled while reducing action. In addition, it has a stable catalytic activity and easy to modify the structure, and unlike a single active site catalyst has a high activity with high access to the substrate.
- the dinuclear metallocene compound represented by Chemical Formula 1 may be used alone or in combination with a promoter to prepare a polyolefin polymer as a catalyst composition, and in particular, may produce a high molecular weight polyolefin with high activity.
- the elepin homopolymer or the olefin copolymer may be provided by performing a polymerization process by contacting a catalyst composition comprising a binuclear metallocene compound represented by Chemical Formula 1 with a monomer.
- Example 1 After adding nucleic acid solvent (1.0 L) and 1-octene 6.4 mm to the 2 L autoclave reactor, the temperature of the reaction mixture was preheated to 120 ° C.
- the compound of Example 1 (0.5 ⁇ ) treated with triisobutylaluminum compound (10 ⁇ ) followed by dimethylanilinium tetrakis (pentafluorophenyl) borate cocatalyst (10 ⁇ ) in a 25 mL catalyst storage tank . It was added and filled (molar ratio 10 of Al: Ti).
- the 2 L autoclave continuous process reactor was filled with nucleic acid solvent (5.4 kg / h) and 1-butene (8 k ⁇ h), and then the silver at the top of the reactor was preheated to 150 ° C ⁇ Triisobutylaluminum compound (0.05 mmol / min), the compound of Example 1 (0.5
- the binuclear metallocene compound of the present invention is a structure in which a single metallocene compound is connected by a diether chain, and has a high catalytic activity by minimizing unnecessary interaction between metals. Polyolefins having a higher molecular weight can be produced than when using a mononuclear metallocene catalyst.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Transition And Organic Metals Composition Catalysts For Addition Polymerization (AREA)
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP13888205.5A EP2998308B1 (en) | 2013-06-25 | 2013-12-27 | Binucleate metallocene compound and method for preparing same |
CN201380077656.7A CN105308060B (zh) | 2013-06-25 | 2013-12-27 | 双核茂金属化合物及其制备方法 |
US14/895,875 US9434752B2 (en) | 2013-06-25 | 2013-12-27 | Dinuclear metallocene compound, and a method for preparing the same |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR20130073043 | 2013-06-25 | ||
KR10-2013-0073043 | 2013-06-25 | ||
KR1020130165067A KR101600583B1 (ko) | 2013-06-25 | 2013-12-27 | 이핵 메탈로센 화합물, 및 이의 제조방법 |
KR10-2013-0165067 | 2013-12-27 |
Publications (1)
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Cited By (4)
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EP3000817A4 (en) * | 2013-06-25 | 2017-03-08 | LG Chem, Ltd. | Catalyst composition, method for preparing same, and method for preparing polyolefins using same |
CN106543317A (zh) * | 2015-09-18 | 2017-03-29 | 中国石油天然气股份有限公司 | 异双核杂环催化剂及其在乙烯聚合中的应用 |
CN106543302A (zh) * | 2015-09-18 | 2017-03-29 | 中国石油天然气股份有限公司 | 双核杂环催化剂及其在丙烯均聚和共聚中的应用 |
EP3053954A4 (en) * | 2013-10-30 | 2017-07-05 | LG Chem, Ltd. | Olefin resin |
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KR102011927B1 (ko) * | 2015-02-05 | 2019-08-19 | 주식회사 엘지화학 | 촉매 조성물 및 이를 이용한 폴리올레핀의 제조방법 |
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US9434752B2 (en) | 2016-09-06 |
EP2998308B1 (en) | 2017-11-29 |
KR101600583B1 (ko) | 2016-03-08 |
EP2998308A1 (en) | 2016-03-23 |
US20160108069A1 (en) | 2016-04-21 |
CN105308060A (zh) | 2016-02-03 |
EP2998308A4 (en) | 2017-02-15 |
KR20150000812A (ko) | 2015-01-05 |
CN105308060B (zh) | 2018-04-24 |
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