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Asymmetric bridged indenocene-based transition metal catalyst, preparation method and application

A technology of indenyl and transition metals, applied in the field of metallocene catalysts, can solve theoretical and technical problems

Active Publication Date: 2022-02-01
CHINA PETROLEUM & CHEM CORP +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

my country's polypropylene products are basically produced using traditional Natta-type catalysts, and some catalysts are added with simple metallocene compound components. There are basically no reports on the use of metallocene compounds as catalysts, because there are still There are theoretical and technical difficulties

Method used

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  • Asymmetric bridged indenocene-based transition metal catalyst, preparation method and application
  • Asymmetric bridged indenocene-based transition metal catalyst, preparation method and application
  • Asymmetric bridged indenocene-based transition metal catalyst, preparation method and application

Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0051] The preparation of the metallocene compound as formula 1:

[0052] Weigh 40mmol of 4-phenyl-2-methylindenyl, dissolve in 200ml Et 2 O, cooled to -78°C, and 40 mmol of 2.4M n-butyllithium in hexane solution was slowly added dropwise thereto, and the dropwise addition was completed over 15 minutes. Return to room temperature naturally under stirring, and stir at room temperature for another 12 h to obtain a solution of indenyllithium compound.

[0053] Weigh 20mmol of Me(PhMeNH 2 CH 2 CH 2 C) SiCl 2 , was dissolved in 100 mL of n-hexane, cooled to -78°C, and the solution of the indenyllithium compound prepared above was slowly added dropwise thereto, and the dropwise addition was completed within 30 minutes. Return to room temperature naturally under stirring, and stir at room temperature for another 12 h. The insolubles are removed by filtration, and the filtrate is passed through a silica gel column to obtain a yellow solution, and the solvent is drained to obtain...

Embodiment 1

[0060] 1. Preparation of catalyst

[0061] Weigh 2 g of silica gel that has been roasted at 600° C., add 10 mL of 10% MAO toluene solution (percentage by weight), and heat to 80° C. Add the toluene solution of the metallocene compound shown in Formula 1 under the condition of uniform stirring, control the Al / Zr ratio to 200:1, and react overnight. The solid was collected by filtration and washed with toluene until the washed solvent was colorless. The solid was dried in vacuum for 24 hours to obtain a solid powder, which was stored in a glove box for future use (this reaction method is used unless otherwise specified below). The catalyst SC-1 with a certain metal content can be obtained by measuring and calculating the amount of feed and the metal content of the washing effluent, wherein the zirconium content is 0.268% (29.4 μmol / g).

[0062]

[0063] 2. Catalytic reaction

[0064] A 300mL autoclave was selected, evacuated in an oil bath at 100°C, and replaced with nitrog...

Embodiment 2 4

[0070] 1. Preparation of catalyst

[0071] Weigh 2 g of silica gel that has been roasted at 600°C, add 10mL of 10% MAO toluene solution (weight percent) and pure toluene solvent, heat to 80°C, stir for 24 hours, filter, collect the solid, and wash it with toluene solvent 3 times, the solid After vacuum drying for 24 hours, MAO-silica gel was obtained as solid powder.

[0072] Weigh a certain amount of MAO-silica gel, add toluene solvent to form a suspension, add the toluene solution of the metallocene zirconium compound under the condition of uniform stirring, and react overnight. The solid was collected by filtration and washed with toluene until the washed solvent was colorless. The solid was dried in vacuum for 24 hours to obtain a solid powder, which was stored in a glove box for future use. A catalyst with a certain zirconium content can be obtained through the measurement and calculation of the feeding amount and the zirconium content of the washing liquid.

[0073] Se...

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Abstract

The invention discloses an asymmetric bridging indenyl transition metal catalyst, a preparation method and an application. The catalyst is produced by combining a metallocene compound, a cocatalyst and a carrier, wherein the metallocene compound is regulated and linked by an asymmetric bridging group to make it easy to assume a racemic structure. The catalyst has good thermal stability and catalytic activity, and can prepare high stereoisotactic metallocene polypropylene. The tacticity of the obtained metallocene polypropylene is >90%, the highest can reach 99.7%, and the number average molecular weight is 10 4 -10 6 Between Daltons, the molecular weight distribution is between 1.5-3.5, and the melting point is in the range of 140-165°C. The produced high isotactic polypropylene has industrial application prospect.

Description

technical field [0001] The invention relates to the field of metallocene catalysts, and relates to an asymmetric bridging indenyl transition metal catalyst, a preparation method and an application thereof. Background technique [0002] Metallocene polypropylene (mPP) has shown good application in fiber, injection molding and film products, and the market demand has increased year by year in recent years. These resin products have high requirements on the stereoregular structure of polypropylene, and the structure of polypropylene is regulated by the structure of the catalyst. [0003] Metallocene polypropylene with high isotactic structure is one of the important resin species, which is synthesized by controlling the growth of propylene chain through the catalyst stereoenantiomer site. Catalysts capable of enantiostatically controlled chain growth reactions need to have C2 axis or lower C1 axis symmetry (Chem.Rev.2000,100,1223), bridged bisindene ring type with racemic stru...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F110/06C08F4/6592
CPCC08F110/06C08F4/65927
Inventor 尹兆林曹育才梁胜彪朱红平叶晓峰倪晨陈志康钟东文宋莎蒋文军刘振宇
Owner CHINA PETROLEUM & CHEM CORP