CN1556117A - Preparation method of mesohole molecular sieve loaded post transition metal olefine polymerization catalyst - Google Patents
Preparation method of mesohole molecular sieve loaded post transition metal olefine polymerization catalyst Download PDFInfo
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- CN1556117A CN1556117A CNA2003101229950A CN200310122995A CN1556117A CN 1556117 A CN1556117 A CN 1556117A CN A2003101229950 A CNA2003101229950 A CN A2003101229950A CN 200310122995 A CN200310122995 A CN 200310122995A CN 1556117 A CN1556117 A CN 1556117A
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- molecular sieve
- transition metal
- olefin polymerization
- metal catalyst
- late transition
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Abstract
A mesoporous molecular sieve carried post-transition metal catalyst for olefin polymerization is composed of components A and B. Component A is JK-Cat(MLX2)-PC, where JK is mesoporous molecular sieve SBA-15, PC is its carrying type, Cat is said catalyst, M is chosen from Fe, Co, Ni and Pd, L is chosen from two-tooth and three-tooth organic ligand, and X is chosen from Cl and Br. Component B is methyl aloxane. It has high catalytic activity.
Description
Technical field
The invention belongs to the preparation method of carrier late transition metal catalyst for olefin polymerization, be specifically related to the late transition metal catalyst for olefin polymerization of meso-porous molecular sieve material load.
Background technology
The polymerization technique process (as the vapour phase polymerization slurry polymerization) that modern industrialization is produced has determined homogeneous catalyst must want carrierization, and the carrierization of current homogeneous catalyst has become one of important directions of olefinic polymerization catalysis.The carrierization of olefin polymerization catalysis is meant a kind of or some kinds of surfaces that transition metal complex is stated from inorganic solid surface or superpolymer, and a certain amount of alkylaluminoxane of load, make the effective constituent (Primary Catalysts, promotor) of catalyzer be adsorbed in the process of solid surface.The carrierization of catalyzer can be improved the performance of catalyzer from many aspects.Supported catalysts is active high with homogeneous catalyst, reaction is fast, condition temperature narrow molecular weight distribution and the different-phase catalyst active centre is stable, product is easily separated, can adapt to characteristics such as multiple manufacturing condition, solve the difficult problem that homogeneous catalyst faces preferably.
It is the chromium-based catalysts of carrier with silica gel in late 1950s that the load of olefin polymerization catalysis starts from the Philips oil company.Nineteen sixty-eight is representative with Montedison company, has developed with MgCl
2Be the titanium catalyst system of carrier, the New Times of having started high-effective carrier catalyst, this has produced far-reaching influence in the polycoordination research field.In order to make the olefin polymerization catalysis performance ideal usefulness of loadization, need investigate physical properties such as intensity, density, total pore volume, pore distribution, aperture, granularity and the particle shape of carrier in earnest, otherwise can not get the ideal carrier catalyzer that performance is applicable to actual production technology.Up to the present, operable carrier is a variety of.On big classification, be divided into inorganic carrier and polymer support two classes.Use in the inorganic carrier relatively extensively, effect is more satisfactory that SiO is arranged
2, MgCl
2, Al
2O
3These three kinds.The most widely used polystyrene support that surely belongs in the organic polymer carrier, in addition, crosslinked polystyrene-acrylamide, crosslinked polystyrene-4-vinylpridine and cyclodextrin also have report.
The mesopore molecular sieve that twentieth century nineties rises has become the focus of catalyticing research as MCM41, SBA etc.Japan Aida research group (Science.1999,285,2113; Macromolecules, 1998,31,4069-73) utilize mesopore molecular sieve MCM-41 that metallocene catalyst has been done a large amount of carrier work, obtained the satisfied result of many people in addition.The novel mesoporous molecular sieve SBA-15 of Chu Xianing has the character of many uniquenesses at the end of last century, as, high-specific surface area, narrow pore size distribution, wide aperture (7-8nm), the high mechanical strength that large pore volume and heavy wall keep is a kind of very ideal support of the catalyst.Because the high-sequential of mesoporous material, the form of the polymkeric substance that obtains certainly will change to some extent owing to the masterplate effect.Up to the present, the report that does not have SBA-15 loaded late transition metal olefin polymerization catalysis.
Summary of the invention
The purpose of this invention is to provide a kind of mesoporous molecular sieve carried late transition metal catalyst for olefin polymerization.
Another object of the present invention provides a kind of preparation method of mesoporous molecular sieve carried late transition metal catalyst for olefin polymerization.
This method is to adopt the method for physical adsorption or chemisorption that late transition metal catalyst is fixed in the duct of mesopore molecular sieve, makes catalyzer bring into play polymerization activity in a constrained environment, to improve the form of polymkeric substance.
The 3rd purpose of the present invention provides a kind of mesoporous molecular sieve carried late transition metal catalyst for olefin polymerization in olefinic polymerization, the especially application in vinyl polymerization.
The catalyzer of the present invention's preparation is made of the expression formula of A component [JK-Cat (MLX A and B two portions
2)-PC], wherein JK represents meso-porous molecular sieve material SBA-15, PC represents the carrying method type, be physical adsorption or chemisorption, Cat represents late transition metal catalyst for olefin polymerization, and M represents iron, cobalt, nickel or palladium wherein any one, L represent bidentate or three tooth organic ligands wherein any one, X represents halogen Cl or Br.The concrete structure of Cat is as follows:
R wherein
1, R
2, R
3, R
4, R
5, R
6, R
7, R
8, R
9, R
10Be H, Me,
iPr,
tBu, Ph, Phen, Anth, Trityl, TPhen, OMe, NO
2, F, Cl, Br wherein any one; M
1Be Fe or Co; M
2Be Ni or Pd; X is Cl or Br;
For
Wherein any one, R
11, R
12Be H, Me, Et,
iPr,
tBu, Ph wherein any one; The B component is methylaluminoxane (MAO), modified methylaluminoxane (MMAO), B (C
6F
5)
3Wherein any one.The all available prior art of such catalyzer makes.
The preparation process of carried catalyst A component is as follows:
1, physical load: with mesoporous molecular sieve SBA-15, at 150-160 ℃ of following vacuum heat-preserving 6-8 hour, behind the cool to room temperature, add toluene, every gram mesopore molecular sieve 45-55mL toluene, under stirring state, add the toluene solution (mesoporous molecular sieve SBA-15/late transition metal catalyst for olefin polymerization weight ratio is 1/0.01-0.2) that is dissolved with late transition metal catalyst for olefin polymerization, stirred respectively under the room temperature 0.5-20 hour, solution colour does not have considerable change, filters, and uses toluene wash 3 times, the toluene consumption is every mol sieve 45-55mL, and vacuum-drying gets the carried catalyst A component of physical adsorption method load; Mesoporous molecular sieve SBA-15/late transition metal catalyst for olefin polymerization weight ratio is 1/0.01-0.2.
The toluene solution concentration of catalyzer is 0.1-10g/mL.
2, chemical load: with mesoporous molecular sieve SBA-15 (-5 kilograms of 1.0 grams), at 150-160 ℃ of following vacuum heat-preserving 6-8 hour, behind the cool to room temperature, add toluene, every gram mesopore molecular sieve 45-55mL toluene under stirring state, adds the toluene solution (10-1000ml) that is dissolved with late transition metal catalyst for olefin polymerization, stir under the room temperature and add lithium alkylide, as lithium methide, n-Butyl Lithium, tert-butyl lithium etc., solution colour changes at once, continue to stir 20-30 minute, and filtered, with toluene wash to 3 time, the toluene consumption is every mol sieve 45-55mL, and vacuum-drying gets the carried catalyst A component of chemisorption method load.Mesoporous molecular sieve SBA-15/late transition metal catalyst for olefin polymerization weight ratio is 1/0.01-0.2, and the amount ratio of catalyzer and lithium alkylide (mol ratio) is 1/1.
The used lithium alkylide of chemical load can be any of lithium methide, n-Butyl Lithium, tert-butyl lithium.
The cocatalyst B component of A component, B component are methylaluminoxane (MAO), improvement methylaluminoxane (MMAO) or penta phenyl fluoride boron [B (C
6F
5)
3] effect under, catalysis in olefine polymerization under 1-20 normal atmosphere.
The present invention makes carrier with mesoporous molecular sieve SBA-15, uses physics or chemiadsorption carry out carrierizations respectively to rear transition metal such as nickel, palladium, iron or cobalt olefin polymerization catalysis, has tested the olefin polymerizating activity of supported catalysts simultaneously.This carrying method improves catalytic activity to realizing the controllable polymerization of back transition olefin polymerization catalysis, obtains the polymkeric substance of desired molecular weight, the degree of branching and linear pattern, and adapting to industrial production device has certain meaning.
The sudden and violent poly-exothermic phenomenon of similar homogeneous catalyst does not appear in characteristics such as it is stable all to show air inlet during the late transition metal catalyst for olefin polymerization olefin polymerization of mesoporous molecular sieve SBA-15 load, and polymerization is mild.The activity of physical adsorption carried catalyst will be higher than the chemical load method.Simultaneously, the sequential 2 D pore passage structure of SBA-15 can be controlled the relative position between the macromolecular chain really.Owing to be masterplate during polymer growth with the molecular sieve, and SBA-15 has the nano level aperture, can limit the direction and the size of olefinic polymerization effectively, the polyolefine that supported catalysts obtains is a nano-scale fiber shaped polymer product, and this is that other class carrier is incomparable.
Embodiment
Embodiment 1: the preparation of carried catalyst A component
Take by weighing mesoporous molecular sieve SBA-15 (0.4g), 160 ℃ of following vacuum heat-preservings 8 hours.Behind the cool to room temperature, add 20mL toluene.Under stirring state, add be dissolved with 0.052g diimine nickel catalyzer [2,6-
IsoPr
2(C
6H
3) N=C (C
10H
6) C=N (C
6H
3) Pr
Iso-2,6] NiBr
2Toluene solution.Stir 0.5hr under the room temperature respectively, solution colour does not have considerable change.Filter, use toluene wash 3 times, vacuum-drying gets the light red carried catalyst, and it is 1.58mg Ni/ (g Polymer) that ICP measures nickel content.
Embodiment 2: the preparation of carried catalyst A component
With taking by weighing mesoporous molecular sieve SBA-15 (0.4g), 160 ℃ of following vacuum heat-preservings 8 hours.Behind the cool to room temperature, add 20mL toluene.Under stirring state, add be dissolved with 0.052g diimine nickel catalyzer [2,6-
IsoPr
2(C
6H
3) N=C (C
10H
6) C=N (C
6H
3) Pr
Iso-2,6] NiBr
2Toluene solution.Stir 20hr under the room temperature respectively, solution colour does not have considerable change.Filter, use toluene wash 3 times, vacuum-drying gets the light red carried catalyst, and it is 3.47mg Ni/ (g Polymer) that ICP measures nickel content.
Embodiment 3: the preparation of carried catalyst A component
Take by weighing mesoporous molecular sieve SBA-15 (0.4g), 160 ℃ of following vacuum heat-preservings 8 hours.Behind the cool to room temperature, add 20mL toluene.Under stirring state, add be dissolved with 0.052g diimine nickel catalyzer [2,6-
IsoPr
2(C
6H
3) N=C (C
10H
6) C=N (C
6H
3) Pr
Iso-2,6] NiBr
2Toluene solution.Stir under the room temperature and add n-Butyl Lithium after 30 minutes (1mL, 1.6mmol), solution colour becomes furvous by redness at once.Continue to stir 30 minutes, and filtered, with toluene wash to 3 time, vacuum-drying gets the grey carried catalyst, and it is 7.30mg Ni/ (gPolymer) that ICP measures nickel content.
Embodiment 4: the preparation of carried catalyst A component
Take by weighing mesoporous molecular sieve SBA-15 (0.4g), 160 ℃ of following vacuum heat-preservings 8 hours.Behind the cool to room temperature, add 20mL toluene.Under stirring state, add be dissolved with 0.047g diimine pyridine iron catalyzer [2,6-
IsoPr
2(C
6H
3) N=CMe (C
5H
3N) CMe=N (C
6H
3) Pr
Iso-2,6] FeCl
2Toluene solution.Stir under the room temperature and add n-Butyl Lithium after 30 minutes (1mL, 1.6mmol), solution colour becomes furvous by redness at once.Continue to stir 30 minutes, and filtered, with toluene wash to 3 time, vacuum-drying gets the grey carried catalyst, and it is 5.88mg Fe/ (g Polymer) that ICP measures iron level.
Embodiment 5: the ethene heterogeneous polymerization
Vinyl polymerization carries out under the anhydrous and oxygen-free condition, the supporter nickel catalyst 68.7mg (1.85 μ molNi) (pressing Al/M=2500), the ethene that add toluene 50ml, promotor methylaluminoxane 2.1ml according to this in reaction system, are obtained by embodiment 1 reacted 0.5 hour in 14 ℃, with the ethanolic soln termination reaction that contains 1% hydrochloric acid, products therefrom is filtered, with washing with alcohol 3 times, and, getting polyethylene 0.80g in 40 ℃ of vacuum-dryings 24 hours, activity is 8.58 * 105g PE/ (mol Ni h).
Embodiment 6: the ethene heterogeneous polymerization
Vinyl polymerization carries out under the anhydrous and oxygen-free condition, the carried catalyst 31.0mg (1.83 μ molNi) (pressing Al/M=2500), the ethene that add toluene 50ml, promotor methylaluminoxane 2.1ml according to this in reaction system, are obtained by embodiment 2 reacted 0.5 hour in 14 ℃, with the ethanolic soln termination reaction that contains 1% hydrochloric acid, products therefrom is filtered, with washing with alcohol 3 times, and, getting polyethylene 0.45g in 40 ℃ of vacuum-dryings 24 hours, activity is 4.95 * 10
5G PE/ (molNi h).
Embodiment 7: the ethene heterogeneous polymerization
Vinyl polymerization carries out under the anhydrous and oxygen-free condition, the supporter nickel catalyst 21.8mg (1.29 μ molNi) (pressing Al/M=2500), the ethene that add toluene 50ml, promotor methylaluminoxane 1.5ml according to this in reaction system, are obtained by embodiment 2 reacted 0.5 hour in 14 ℃, with the ethanolic soln termination reaction that contains 1% hydrochloric acid, products therefrom is filtered, with washing with alcohol 3 times, and, getting polyethylene 0.39g in 40 ℃ of vacuum-dryings 24 hours, activity is 6.06 * 10
5G PE/ (mol Ni h).
Embodiment 8: the ethene heterogeneous polymerization
Vinyl polymerization carries out under the anhydrous and oxygen-free condition, the supporter nickel catalyst 14.0mg (1.74 μ molNi) (pressing Al/M=2500), the ethene that add toluene 50ml, promotor methylaluminoxane 2.0ml according to this in reaction system, are obtained by embodiment 3 reacted 0.5 hour in 14 ℃, with the ethanolic soln termination reaction that contains 1% hydrochloric acid, products therefrom is filtered, with washing with alcohol 3 times, and, getting polyethylene 0.19g in 40 ℃ of vacuum-dryings 24 hours, activity is 2.24 * 10
5G PE/ (mol Ni h).
Embodiment 9: the ethene heterogeneous polymerization
Vinyl polymerization carries out under the anhydrous and oxygen-free condition, the carrier iron catalyst 17.0mg (1.79 μ molNi) (pressing Al/M=1600), the ethene that add toluene 50ml, promotor methylaluminoxane 1.3ml according to this in reaction system, are obtained by embodiment 3 reacted 0.5 hour in 14 ℃, with the ethanolic soln termination reaction that contains 1% hydrochloric acid, products therefrom is filtered, with washing with alcohol 3 times, and, getting polyethylene 0.18g in 40 ℃ of vacuum-dryings 24 hours, activity is 1.88 * 10
5G PE/ (mol Fe h).
Claims (6)
1. mesoporous molecular sieve carried late transition metal catalyst for olefin polymerization is characterized in that catalyzer is made of the expression formula of A component [JK-Cat (MLX A and B two components
2)-PC], JK is meso-porous molecular sieve material SBA-15, PC is the carrying method type, can be chemical load or physical load, Cat is a late transition metal catalyst for olefin polymerization, M be iron, cobalt, nickel, palladium wherein any one, L be bidentate or three tooth organic ligands wherein any one, X is halogen Cl or Br; The B component be methylaluminoxane, modified methylaluminoxane, penta phenyl fluoride boron wherein any one.
2. the preparation method of mesoporous molecular sieve carried late transition metal catalyst for olefin polymerization according to claim 1 is characterized in that the physical load method is: with mesoporous molecular sieve SBA-15 at 150-160 ℃ of following vacuum heat-preserving 6-8 hour; Be cooled to room temperature, add in the toluene; Add the toluene solution that is dissolved with late transition metal catalyst for olefin polymerization then, stirred 0.5-20 hour under the room temperature, filter, washing gets final product, the toluene consumption of wherein every gram mesopore molecular sieve is 45-55mL, and mesoporous molecular sieve SBA-15/late transition metal catalyst for olefin polymerization weight ratio is 1/0.01-0.2.
3, the preparation method of mesoporous molecular sieve carried late transition metal catalyst for olefin polymerization according to claim 2, the toluene solution concentration of catalyzer is 0.1-10g/mL when it is characterized in that physical load.
4, the preparation method of mesoporous molecular sieve carried late transition metal catalyst for olefin polymerization according to claim 1 is characterized in that the chemical load method is: with mesoporous molecular sieve SBA-15 at 150-160 ℃ of following vacuum heat-preserving 6-8 hour; Be cooled to room temperature, add toluene solvant, add then and be dissolved with the late transition metal catalyst for olefin polymerization mole) toluene solution, add lithium alkylide under the room temperature, stirred washing, dry getting final product 20-30 minute, mesoporous SBA-15/ late transition metal catalyst for olefin polymerization weight ratio is 1/0.01-0.2, and the consumption mol ratio of catalyzer and lithium alkylide is 1/1.
5, the preparation method of mesoporous molecular sieve carried late transition metal catalyst for olefin polymerization according to claim 4, the lithium alkylide when it is characterized in that chemical load is any in lithium methide, n-Butyl Lithium, the tert-butyl lithium.
6, according to claim 1,2, the 4 described mesoporous molecular sieve carried application of late transition metal catalyst for olefin polymerization in vinyl polymerization.
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100341904C (en) * | 2005-07-21 | 2007-10-10 | 浙江大学 | Method of preparing nano-polyethylene fiber by normal pressure extrusion polymerization |
| CN101288851B (en) * | 2007-04-20 | 2011-04-13 | 南京大学 | SBA-15 loaded high dispersion nickel catalyst modified by hole wall carbon and its preparation method |
| CN102453134A (en) * | 2010-10-19 | 2012-05-16 | 中国石油化工股份有限公司 | Olefin polymerization method |
| CN102453139A (en) * | 2010-10-19 | 2012-05-16 | 中国石油化工股份有限公司 | Olefin polymerization method |
| CN102631946A (en) * | 2012-04-09 | 2012-08-15 | 复旦大学 | IVB group (N, N, O, O) complex olefin polymerization catalyst, preparation method thereof and application |
| CN103889938A (en) * | 2011-10-31 | 2014-06-25 | 埃克森美孚化学专利公司 | Olefin oligomerization process |
-
2003
- 2003-12-30 CN CN 200310122995 patent/CN1261464C/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100341904C (en) * | 2005-07-21 | 2007-10-10 | 浙江大学 | Method of preparing nano-polyethylene fiber by normal pressure extrusion polymerization |
| CN101288851B (en) * | 2007-04-20 | 2011-04-13 | 南京大学 | SBA-15 loaded high dispersion nickel catalyst modified by hole wall carbon and its preparation method |
| CN102453134A (en) * | 2010-10-19 | 2012-05-16 | 中国石油化工股份有限公司 | Olefin polymerization method |
| CN102453139A (en) * | 2010-10-19 | 2012-05-16 | 中国石油化工股份有限公司 | Olefin polymerization method |
| CN102453134B (en) * | 2010-10-19 | 2013-07-03 | 中国石油化工股份有限公司 | Olefin polymerization method |
| CN102453139B (en) * | 2010-10-19 | 2013-09-25 | 中国石油化工股份有限公司 | Olefin polymerization method |
| CN103889938A (en) * | 2011-10-31 | 2014-06-25 | 埃克森美孚化学专利公司 | Olefin oligomerization process |
| CN103889938B (en) * | 2011-10-31 | 2016-08-17 | 埃克森美孚化学专利公司 | Alkene oligomerization process |
| CN102631946A (en) * | 2012-04-09 | 2012-08-15 | 复旦大学 | IVB group (N, N, O, O) complex olefin polymerization catalyst, preparation method thereof and application |
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|---|---|
| CN1261464C (en) | 2006-06-28 |
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