WO2007119936A1 - Method for polymerization and copolymerization of olefin - Google Patents
Method for polymerization and copolymerization of olefin Download PDFInfo
- Publication number
- WO2007119936A1 WO2007119936A1 PCT/KR2007/001453 KR2007001453W WO2007119936A1 WO 2007119936 A1 WO2007119936 A1 WO 2007119936A1 KR 2007001453 W KR2007001453 W KR 2007001453W WO 2007119936 A1 WO2007119936 A1 WO 2007119936A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- polymerization
- copolymerization
- catalyst
- olefin
- titanium
- Prior art date
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- 238000006116 polymerization reaction Methods 0.000 title claims abstract description 35
- 238000000034 method Methods 0.000 title claims abstract description 32
- 150000001336 alkenes Chemical class 0.000 title claims abstract description 26
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 title claims abstract description 21
- 238000007334 copolymerization reaction Methods 0.000 title claims abstract description 17
- 239000003054 catalyst Substances 0.000 claims abstract description 65
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 21
- 239000010936 titanium Substances 0.000 claims abstract description 20
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 15
- -1 magnesium halide compound Chemical class 0.000 claims abstract description 10
- 239000007787 solid Substances 0.000 claims abstract description 9
- 150000002681 magnesium compounds Chemical class 0.000 claims abstract description 7
- 229910052749 magnesium Inorganic materials 0.000 claims abstract description 5
- 239000011777 magnesium Substances 0.000 claims abstract description 5
- 239000002904 solvent Substances 0.000 claims abstract description 5
- 150000001298 alcohols Chemical class 0.000 claims abstract description 4
- 239000004215 Carbon black (E152) Substances 0.000 claims abstract description 3
- 150000004292 cyclic ethers Chemical class 0.000 claims abstract description 3
- 229930195733 hydrocarbon Natural products 0.000 claims abstract description 3
- 150000002430 hydrocarbons Chemical class 0.000 claims abstract description 3
- 238000005406 washing Methods 0.000 claims abstract description 3
- 229910052782 aluminium Inorganic materials 0.000 claims abstract 4
- 230000032683 aging Effects 0.000 claims abstract 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract 2
- 230000003028 elevating effect Effects 0.000 claims abstract 2
- 150000002902 organometallic compounds Chemical class 0.000 claims abstract 2
- 229910052760 oxygen Inorganic materials 0.000 claims abstract 2
- 239000001301 oxygen Substances 0.000 claims abstract 2
- 239000002245 particle Substances 0.000 claims abstract 2
- 230000000737 periodic effect Effects 0.000 claims abstract 2
- 239000011877 solvent mixture Substances 0.000 claims abstract 2
- SJJCABYOVIHNPZ-UHFFFAOYSA-N cyclohexyl-dimethoxy-methylsilane Chemical compound CO[Si](C)(OC)C1CCCCC1 SJJCABYOVIHNPZ-UHFFFAOYSA-N 0.000 claims description 7
- ZVMRWPHIZSSUKP-UHFFFAOYSA-N dicyclohexyl(dimethoxy)silane Chemical compound C1CCCCC1[Si](OC)(OC)C1CCCCC1 ZVMRWPHIZSSUKP-UHFFFAOYSA-N 0.000 claims description 2
- JWCYDYZLEAQGJJ-UHFFFAOYSA-N dicyclopentyl(dimethoxy)silane Chemical compound C1CCCC1[Si](OC)(OC)C1CCCC1 JWCYDYZLEAQGJJ-UHFFFAOYSA-N 0.000 claims description 2
- VHPUZTHRFWIGAW-UHFFFAOYSA-N dimethoxy-di(propan-2-yl)silane Chemical compound CO[Si](OC)(C(C)C)C(C)C VHPUZTHRFWIGAW-UHFFFAOYSA-N 0.000 claims description 2
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 claims 2
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 claims 2
- 150000001875 compounds Chemical class 0.000 claims 2
- UYXLOULABOHUAJ-UHFFFAOYSA-N CO[SiH](OC)CCC1=CC=CC=C1 Chemical compound CO[SiH](OC)CCC1=CC=CC=C1 UYXLOULABOHUAJ-UHFFFAOYSA-N 0.000 claims 1
- AHUXYBVKTIBBJW-UHFFFAOYSA-N dimethoxy(diphenyl)silane Chemical compound C=1C=CC=CC=1[Si](OC)(OC)C1=CC=CC=C1 AHUXYBVKTIBBJW-UHFFFAOYSA-N 0.000 claims 1
- NHYFIJRXGOQNFS-UHFFFAOYSA-N dimethoxy-bis(2-methylpropyl)silane Chemical compound CC(C)C[Si](OC)(CC(C)C)OC NHYFIJRXGOQNFS-UHFFFAOYSA-N 0.000 claims 1
- CVQVSVBUMVSJES-UHFFFAOYSA-N dimethoxy-methyl-phenylsilane Chemical compound CO[Si](C)(OC)C1=CC=CC=C1 CVQVSVBUMVSJES-UHFFFAOYSA-N 0.000 claims 1
- OANIYCQMEVXZCJ-UHFFFAOYSA-N ditert-butyl(dimethoxy)silane Chemical compound CO[Si](OC)(C(C)(C)C)C(C)(C)C OANIYCQMEVXZCJ-UHFFFAOYSA-N 0.000 claims 1
- FWDBOZPQNFPOLF-UHFFFAOYSA-N ethenyl(triethoxy)silane Chemical compound CCO[Si](OCC)(OCC)C=C FWDBOZPQNFPOLF-UHFFFAOYSA-N 0.000 claims 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims 1
- HXLWJGIPGJFBEZ-UHFFFAOYSA-N tert-butyl(trimethoxy)silane Chemical compound CO[Si](OC)(OC)C(C)(C)C HXLWJGIPGJFBEZ-UHFFFAOYSA-N 0.000 claims 1
- XYJRNCYWTVGEEG-UHFFFAOYSA-N trimethoxy(2-methylpropyl)silane Chemical compound CO[Si](OC)(OC)CC(C)C XYJRNCYWTVGEEG-UHFFFAOYSA-N 0.000 claims 1
- ZNOCGWVLWPVKAO-UHFFFAOYSA-N trimethoxy(phenyl)silane Chemical compound CO[Si](OC)(OC)C1=CC=CC=C1 ZNOCGWVLWPVKAO-UHFFFAOYSA-N 0.000 claims 1
- 230000037048 polymerization activity Effects 0.000 abstract description 5
- 230000000379 polymerizing effect Effects 0.000 abstract 1
- 229920000098 polyolefin Polymers 0.000 abstract 1
- 238000002360 preparation method Methods 0.000 description 19
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 15
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 9
- 229920000642 polymer Polymers 0.000 description 9
- 239000000203 mixture Substances 0.000 description 7
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 5
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 5
- 238000003756 stirring Methods 0.000 description 5
- 239000006228 supernatant Substances 0.000 description 5
- 239000008096 xylene Substances 0.000 description 5
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 4
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 238000003556 assay Methods 0.000 description 2
- MGWAVDBGNNKXQV-UHFFFAOYSA-N diisobutyl phthalate Chemical compound CC(C)COC(=O)C1=CC=CC=C1C(=O)OCC(C)C MGWAVDBGNNKXQV-UHFFFAOYSA-N 0.000 description 2
- 229910001629 magnesium chloride Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 description 2
- VOITXYVAKOUIBA-UHFFFAOYSA-N triethylaluminium Chemical compound CC[Al](CC)CC VOITXYVAKOUIBA-UHFFFAOYSA-N 0.000 description 2
- 239000002841 Lewis acid Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012456 homogeneous solution Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Natural products C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 238000006772 olefination reaction Methods 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000004711 α-olefin Substances 0.000 description 1
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
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F10/02—Ethene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F10/04—Monomers containing three or four carbon atoms
- C08F10/06—Propene
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F10/04—Monomers containing three or four carbon atoms
- C08F10/08—Butenes
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F10/14—Monomers containing five or more carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/65—Pretreating the metal or compound covered by group C08F4/64 before the final contacting with the metal or compound covered by group C08F4/44
- C08F4/652—Pretreating with metals or metal-containing compounds
- C08F4/656—Pretreating with metals or metal-containing compounds with silicon 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
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
- C08F4/65912—Component covered by group C08F4/64 containing a transition metal-carbon bond in combination with an organoaluminium compound
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F4/00—Polymerisation catalysts
- C08F4/42—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors
- C08F4/44—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides
- C08F4/60—Metals; Metal hydrides; Metallo-organic compounds; Use thereof as catalyst precursors selected from light metals, zinc, cadmium, mercury, copper, silver, gold, boron, gallium, indium, thallium, rare earths or actinides together with refractory metals, iron group metals, platinum group metals, manganese, rhenium technetium or compounds thereof
- C08F4/62—Refractory metals or compounds thereof
- C08F4/64—Titanium, zirconium, hafnium or compounds thereof
- C08F4/659—Component covered by group C08F4/64 containing a transition metal-carbon bond
- C08F4/65916—Component covered by group C08F4/64 containing a transition metal-carbon bond supported on a carrier, e.g. silica, MgCl2, polymer
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F110/00—Homopolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
- C08F110/04—Monomers containing three or four carbon atoms
- C08F110/06—Propene
Definitions
- the present invention relates to a method for polymerization and copolymerization of olefin, specifically to a method for polymerization and copolymerization of olefin using a prepolymerized catalyst obtained by prepolymerizing olefins with a solid complex titanium catalyst at low temperature under low pressure.
- Tetrahydrofuran that is a cyclic ether
- a magnesium chloride compound for example in US patent No. 4,482,687
- a cocatalyst for example in US patent No. 4,158,642
- a solvent for example in US patent No. 4,477,639 and the like.
- the present invention has been designed to overcome the problems of prior arts. Accordingly, the object of the present invention is to provide a method for polymerization and copolymerization of olefin, which can provide high polymerization activity and a polymer of high stereoregularity.
- Mode for Invention
- Step 1 Preparation of a magnesium compound solution
- Step 2 Preparation of a carrier
- a 0.5 L high pressure reactor was cleansed with propylene and maintained at 15 °C .
- the xylene soluble assay is one of the methods for determining the isotactic index of polymers, wherein a certain amount of polymer sample is added to a xylene solution and completely dissolved thereinto at high temperature not less than 110 °C , and the resulted solution is cooled to room temperature and filtered. The precipitated materials collected by filtering is separated and measured for the content of xylene solubles.
- the method for polymerization and copolymerization of olefin according to the present invention provides high stereoregularity in the resulted polymers, and improved polymerization activity, thereby improving productivity of the polymerization process.
Abstract
Disclosed is a method for polymerization and copolymerization of olefin characterized by polymerizing or copolymerizing olefins in the presence of: (A) a prepolymerized catalyst obtained by prepolymerizing olefins in the presence of (a) a solid complex titanium catalyst prepared by the following steps, (b) an aluminum alkyl and (c) an electron donor, wherein the steps comprises: (i) preparing a magnesium compound solution by dissolving a magnesium halide compound into an oxygen - containing solvent mixture of a cyclic ether and one or more alcohols; (ii) preparing a carrier by firstly reacting the resulted magnesium compound solution with a titanium halide compound at -10 -30oC, elevating the temperature or aging the resulted product to obtain particles, and secondly reacting the resulted product with a titanium halide compound; (iii) preparing a titanium catalyst by reacting the obtained carrier with a titanium halide compound and an electron donor; and (iv) washing the resulted catalyst with a hydrocarbon solvent at 40 - 200oC; (B) an organometallic compound from Group II or III of Periodic table of elements; and (C) an external electron donor. The method for polymerization and copolymerization of olefin can provide olefin polymers having high stereoregularity, enhanced polymerization activity and improved productivity in a polymerization process.
Description
Description METHOD FOR POLYMERIZATION AND COPOLY-
MERIZATION OF OLEFIN
Technical Field
[1] The present invention relates to a method for polymerization and copolymerization of olefin, specifically to a method for polymerization and copolymerization of olefin using a prepolymerized catalyst obtained by prepolymerizing olefins with a solid complex titanium catalyst at low temperature under low pressure. Background Art
[2] Many catalysts for polymerization of olefin and polymerization methods using the same have been reported so far. However, there still have been needs for more efforts to: improve physical properties of the resulted polymers by using a catalyst invented to have more improved commercial qualities; thus raise productivity; or enhance the product quality, and many demands for improvement in the activity and stereo- regularity of a catalyst itself.
[3] Magnesium - containing and titanium - based catalysts for polymerization of olefin, and methods for producing such catalysts have been reported many. Particularly, methods for preparing a catalyst using a magnesium compound solution have been well known in the art, in order to adjust the shape, size or the like of the catalyst.
[4] For example, there is a method for obtaining a magnesium solution by reacting a magnesium compound with an electron donor such as alcohols, amines, ethers, esters, carboxylic acids and the like, in the presence of a hydrocarbon solvent. Methods using alcohols are disclosed in US patent Nos. 4,330,649 and 5,106,807, and Japanese laid - open patent publication Sho 58-83006. Further, methods for preparing a magnesium solution are also reported in US patent Nos. 4,315,874, 4,399,054 and 4,071,674.
[5] Tetrahydrofuran, that is a cyclic ether, has been variously utilized with a magnesium chloride compound, for example in US patent No. 4,482,687, as an additive for a cocatalyst, for example in US patent No. 4,158,642, as a solvent, for example in US patent No. 4,477,639 and the like.
[6] US patent Nos. 4,347,158, 4,422,957, 4,425,257, 4,618,661 and 4,680,381 suggest methods for preparing a catalyst, in which a Lewis acid compound such as aluminum chloride is added to a supporter, magnesium chloride, and the mixture is ground to prepare a catalyst. Disclosure of Invention Technical Problem
[7] Although the catalyst activity has been improved in above - mentioned patents, there
still have been needs for further improvement regarding the catalyst morphology such as the shape, size, size distribution and stereoregularity of a catalyst.
[8] As it has been described above, the aspects for improving the commercial value of a catalyst for polymerization of alpha-olefin are focused on: efforts to produce a catalyst having a high polymerization activity and stereoregularity so as to enhance the product quality; efforts to control the shape and the size of a catalyst so as to improve productivity; and efforts to improve the production yield and the activity of a catalyst in catalyst preparation so as to save the production cost. These efforts are strongly needed in the art, since they are important factors in catalyst economy. Technical Solution
[9] The present invention has been designed to overcome the problems of prior arts. Accordingly, the object of the present invention is to provide a method for polymerization and copolymerization of olefin, which can provide high polymerization activity and a polymer of high stereoregularity. Mode for Invention
[10] The present invention can be further understood by the following examples, which are provided to illustrate the present invention, however by no means limiting the scope to be protected in the present invention.
[11] Examples
[12] Example 1
[13] Preparation of a prepolymerized catalyst (A)
[14] Step 1 : Preparation of a magnesium compound solution
[15] To a 500 L reactor equipped with a mechanical stirrer of which atmosphere was substituted with nitrogen, 15kg of MgCl , 225kg of toluene, 17kg of tetrahydrofuran and 31 kg of butanol were added. The mixture was heated to 110 °C with stirring at 70 rpm, and maintained at the temperature for 3 hours to obtain a homogeneous solution.
[16] Step 2 : Preparation of a carrier
[17] The solution obtained from the above step 1 was cooled to 17 °C and 32kg of TiCl was added thereto. The temperature of the reactor was elevated to 60 °C over 1 hour. When the temperature reached to 60 °C , 13kg of TiCl 4 was added to the reactor over
40 minutes and allowed it for reaction for further 30 minutes. After the reaction, it was allowed to stand for 30 minutes to settle the resulted carriers, and the upper part of the solution was removed. To the residual slurry in the reactor, 90kg of toluene was added, and the mixture was washed by repeating the series of steps of stirring, standing and removal of the supernatant, three times.
[18] Step 3: Preparation of a solid complex titanium catalyst
[19] To the carrier prepared from the above step 2, 80kg of toluene and 90 kg of TiCl 4
were added with stirring at the speed of 60 rpm. The reactor temperature was elevated to 110 °C over 1 hour, and the mixture was aged for 1 hour and allowed to stand for 15 minutes so as to settle precipitates, and the resulted supernatant was separated. To the remained slurry, 87 kg of toluene, 52 kg of TiCl 4 and 4.2 kg of diisobutylphthalate were added, and the temperature was elevated to 120 °C and maintained 1 hour for further reaction. After the reaction, it was allowed to stand for 30 minutes, and the supernatant was removed. To the reactor, 80 kg of toluene and 76 kg of TiCl 4 were added, and the mixture was reacted at 100 °C for 30 minutes. After the reaction, it was allowed to stand for 30 minutes, and the supernatant was removed. To the residual slurry, 65 kg of hexane was added, and the temperature of the reactor was raised to 60 °C and maintained for 30 minutes while stirring. After halting the stirring, the mixture was allowed to stand for 30 minutes and the supernatant was removed. The residual catalyst slurry was washed by adding hexane thereto, and this washing process was repeated 6 times, thereby obtaining the final solid complex titanium catalyst. The Ti content of the resulted catalyst was 2.8wt%.
[20] Step 4: Prepolymerization
[21] A 0.5 L high pressure reactor was cleansed with propylene and maintained at 15 °C .
To the reactor, 4g of the catalyst obtained from above step 3, 300 D of hexane, 10 mmol of triethylaluminum and 0.5 mmol of cyclohexylmethyldimethoxysilane were added in this order, and the mixture was stirred for 30 minutes. Prepolymerization was carried out at 15 °C for 3 hours, while flowing propylene at the rate of 80 ml/minute. In the prepolymerized catalyst resulted therefrom, the amount of polymers having high molecular weight formed around the catalyst was 6.8g per g of catalyst.
[22] Polymerization
[23] Polymerization of propylene was carried out in order to estimate the performance of the resulted prepolymerized catalyst. The prepared prepolymerized catalyst was placed in a high pressure bombe, with the amount of 10 mg, based on the solid complex titanium catalyst. The bombe was mounted to a 2L high pressure polymerization reactor, and the reactor was purged with nitrogen for about 1 hour so as to form dry nitrogen atmosphere inside the reactor. Thereto, triethylaluminum (Al/Ti molar ratio = 450) and dicyclohexyldimethoxysilane (Si/Al molar ratio =0.1) as an external donor were added, and the reactor was tightly closed. After feeding 1000 ml of hydrogen, 1200 ml of liquid propylene was fed through a syringe pump, and the temperature of the reactor was raised to 70 °C over 20 minutes. The prepolymerized catalyst was added to the reactor to carry out polymerization for 1 hour. After 1 hour, unreacted propylene was vented out to the air, and the temperature of the reactor was lowered to room temperature. The resulted polymer was dried in a vacuum oven at 50 °C and then weighed. With the resulted polymer, assays regarding xylene solubles and II (NMR
pentad) were conducted, and the results were shown in Table 1. The xylene soluble assay is one of the methods for determining the isotactic index of polymers, wherein a certain amount of polymer sample is added to a xylene solution and completely dissolved thereinto at high temperature not less than 110 °C , and the resulted solution is cooled to room temperature and filtered. The precipitated materials collected by filtering is separated and measured for the content of xylene solubles.
[24] Example 2
[25] Preparation of a prepolymerized catalyst and polymerization were carried out as same as the method disclosed in Example 1, except that 0.7 mmol of cyclohexyl- methyldimethoxysilane was used for preparing the prepolymerized catalyst, in the step 4 of the prepolymerized catalyst preparation method. The results were shown in Table 1.
[26] Example 3
[27] Preparation of a prepolymerized catalyst and polymerization were carried out as same as the method disclosed in Example 1, except that 0.9 mmol of cyclohexyl- methyldimethoxysilane was used for preparing the prepolymerized catalyst, in the step 4 of the prepolymerized catalyst preparation method. The results were shown in Table 1.
[28] Example 4
[29] Preparation of a prepolymerized catalyst and polymerization were carried out as same as the method disclosed in Example 1, except that 0.5 mmol of dicy- clopentyldimethoxysilane was used for preparing the prepolymerized catalyst, in the step 4 of the prepolymerized catalyst preparation method. The results were shown in Table 1.
[30] Example 5
[31] Preparation of a prepolymerized catalyst and polymerization were carried out as same as the method disclosed in Example 1, except that 0.5 mmol of diisopropy- ldimethoxysilane was used for preparing the prepolymerized catalyst, in the step 4 of the prepolymerized catalyst preparation method. The results were shown in Table 1.
[32] Comparative example 1
[33] Preparation of a prepolymerized catalyst and polymerization were carried out as same as the method disclosed in Example 1, except that the electron donor, cyclo- hexylmethyldimethoxysilane was not used for preparing the prepolymerized catalyst, in the step 4 of the prepolymerized catalyst preparation method. The results were shown in Table 1.
[34] Comparative example 2
[35] Preparation of a prepolymerized catalyst and polymerization were carried out as same as the method disclosed in Example 1, except that 3.5 mmol of an electron donor,
cyclohexylmethyldimethoxysilane was used for preparing the prepolymerized catalyst, in the step 4 of the prepolymerized catalyst preparation method. The results were shown in Table 1.
[36] Comparative example 3 [37] Preparation of a prepolymerized catalyst and polymerization were carried out as same as the method disclosed in Example 1, except that 7.0 mmol of an electron donor, cyclohexylmethyldimethoxysilane was used for preparing the prepolymerized catalyst, in the step 4 of the prepolymerized catalyst preparation method. The results were shown in Table 1.
[38] [Table 1] [Table ] Table 1
[39] As it can be seen from the above table 1, the examples according to the polymerization and copolymerization of olefin of the present invention exhibit the reduced amount of xylene solubles in the prepared polymers and improved stereoregularity and polymerization activity, as compared to the comparative examples. Industrial Applicability
[40] The method for polymerization and copolymerization of olefin according to the present invention provides high stereoregularity in the resulted polymers, and improved polymerization activity, thereby improving productivity of the polymerization process.
Claims
[1] L A method for polymerization or copolymerization of olefin which polymerizes or copolymerizes olefins in the presence of (A), (B) and (C):
(A) a prepolymerized catalyst obtained by prepolymerizing olefins in the presence of (a) a solid complex titanium catalyst prepared by the following steps, (b) an aluminum alkyl and (c) an electron donor, wherein the steps comprise:
(i) preparing a magnesium compound solution by dissolving a magnesium halide compound into an oxygen - containing solvent mixture of a cyclic ether and one or more alcohols;
(ii) preparing a carrier by firstly reacting the resulted magnesium compound solution with a titanium halide compound at -10 -30°C elevating the temperature or aging the resulted product to obtain particles, and secondly reacting the resulted product with a titanium halide compound;
(iii) preparing a titanium catalyst by reacting the obtained carrier with a titanium halide compound and an electron donor; and
(iv) washing the resulted catalyst with a hydrocarbon solvent at 40 -200 °C ;
(B) an organometallic compound from Group II or in of Periodic table of elements; and
(C) an external electron donor.
[2] 2. The method for polymerization or copolymerization of olefin according to claim 1, wherein the temperature for prepolymerization is -50 - 50 °C .
[3] 3. The method for polymerization or copolymerization of olefin according to claim 1, wherein the olefin is at least one selected from the group consisting of ethylene, propylene, 1 - butene, 1 - hexene and 1 - octene.
[4] 4. The method for polymerization or copolymerization of olefin according to claim 1, wherein the concentration of (a) the solid complex titanium catalyst in IL of solvent used in the prepolymerization system is 0.01 - 500 mmol, being calculated as titanium atom.
[5] 5. The method for polymerization or copolymerization of olefin according to claim 1, wherein (b) the aluminum alkyl is selected from trialkylaluminum and trialkenylaluminum.
[6] 6. The method for polymerization or copolymerization of olefin according to claim 1, wherein the amount of (b) the aluminum alkyl being used is 1 - 100 mole per mole of titanium atom in (a) the solid complex titanium catalyst.
[7] 7. The method for polymerization or copolymerization of olefin according to claim 1, wherein (c) the electron donor is an alkoxysilane compound.
[8] 8. The method for polymerization or copolymerization of olefin according to
claim 7, wherein the alkoxysilane compound is selected from the group consisting of diphenyldimethoxysilane, phenyltrimethoxysilane, phenylethyldimethoxysilane, phenyl- methyldimethoxysilane, isobutyltrimethoxysilane, diisobutyldimethoxysilane, di- isopropyldimethoxysilane, di - t - butyldimethoxysilane, t - butyltrimethoxysilane, cyclohexylmethyldimethoxysilane, dicy- clopentyldimethoxysilane, dicyclohexyldimethoxysilane, 2 - norbornanetri- ethoxysilane, 2 - norbornanemethyldimetoxysilane and vinyltriethoxysilane. [9] 9. The method for polymerization or copolymerization of olefin according to claim 1, wherein the amount of (c) the electron donor being used is 0.001 - 3 moles per mole of titanium atom in (a) the solid complex titanium catalyst.
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Citations (4)
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EP0912617A1 (en) * | 1997-06-09 | 1999-05-06 | Montell Technology Company bv | Components and catalysts for the polymerization of olefins |
EP1276776A1 (en) * | 2000-04-24 | 2003-01-22 | Samsung General Chemicals Co., Ltd. | Catalyst for producing an ultra high molecular weight polyethylene and method for producing an ultra high molecular weight polyethylene using the same |
EP1353962A1 (en) * | 2000-12-15 | 2003-10-22 | Basell Poliolefine Italia S.p.A. | Continuous process for the preparation of solid catalyst components for the polymerisation of alpha-olefins |
EP1360210A1 (en) * | 2000-12-27 | 2003-11-12 | Samsung General Chemicals Co., Ltd. | Method of homo- or co-polymerization of $g(a)-olefin |
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US4347158A (en) | 1980-05-02 | 1982-08-31 | Dart Industries, Inc. | Supported high efficiency polyolefin catalyst component and methods of making and using the same |
US4425257A (en) | 1980-05-02 | 1984-01-10 | Phillips Petroleum Company | Supported high efficiency polyolefin catalyst component and methods of making and using the same |
US4422957A (en) | 1980-05-02 | 1983-12-27 | Phillips Petroleum Company | Methods of producing polyolefins using supported high efficiency polyolefin catalyst components |
US5166340A (en) | 1989-07-26 | 1992-11-24 | Himont Incorporated | Organosilane compounds |
JPH04347158A (en) * | 1991-05-24 | 1992-12-02 | Matsushita Electric Ind Co Ltd | Jetting port for jet flow bath apparatus |
JPH05166340A (en) * | 1991-12-17 | 1993-07-02 | Nec Corp | Magnetic head arm assembly |
JPH0780395A (en) * | 1993-09-09 | 1995-03-28 | Nippon Steel Corp | Coating method of plate material |
JP3845675B2 (en) * | 2001-03-13 | 2006-11-15 | 独立行政法人科学技術振興機構 | Nucleic acid separating agent |
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Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
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EP0912617A1 (en) * | 1997-06-09 | 1999-05-06 | Montell Technology Company bv | Components and catalysts for the polymerization of olefins |
EP1276776A1 (en) * | 2000-04-24 | 2003-01-22 | Samsung General Chemicals Co., Ltd. | Catalyst for producing an ultra high molecular weight polyethylene and method for producing an ultra high molecular weight polyethylene using the same |
EP1353962A1 (en) * | 2000-12-15 | 2003-10-22 | Basell Poliolefine Italia S.p.A. | Continuous process for the preparation of solid catalyst components for the polymerisation of alpha-olefins |
EP1360210A1 (en) * | 2000-12-27 | 2003-11-12 | Samsung General Chemicals Co., Ltd. | Method of homo- or co-polymerization of $g(a)-olefin |
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