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Modified particles, catalyst for olefin polymerization using the same, and process of producing olefin polymer

A technology for olefin polymerization and compounds, applied in chemical instruments and methods, inorganic pigment treatment, fibrous fillers, etc., can solve problems such as easy changes in copolymers

Inactive Publication Date: 2006-12-20
SUMITOMO CHEM CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] In addition, these metallocene catalysts have a disadvantage that the properties (such as density, melting point, etc.) of the copolymers obtained by changing the ratio of monomers in the polymerization reaction are easy to change, because there are a large number of short chain branches (SCB) in the copolymer products.

Method used

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Examples

Experimental program
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Effect test

preparation example Construction

[0097] In the preparation of the modified particles of the present invention, in the particles obtained by contacting (a) with (b) in terms of the number of moles of the atoms contained in 1 g of the particles, taking into account the amount of (b) to (a) The amount of atoms of the metal compound (b) contained is preferably 0.1 mmol or more, more preferably in the range of 0.5 to 20 mmol. Considering the amount of (c), the molar ratio [(c) / (b)] of the atoms of the compound (c) to the metal compound (b) contained in 1 g of the particles is preferably 0.01-100, more preferably 0.05- 20, especially preferably in the range of 0.1-10, the compound (c) bears an active hydrogen-containing functional group or an aproton-donating basic functional group and an electron withdrawing group.

[0098] The modified particles of the present invention can be used as carriers for supporting catalyst components for olefin polymerization such as transition metal compounds, and are preferably used ...

Embodiment 1

[0149] (1) Preparation of modified particles

[0150] A 50 ml four-necked flask equipped with a stirrer, dropping funnel and thermometer was dried under reduced pressure, and then the air in the flask was replaced with nitrogen. The flask was filled with 1.02 g of silica (manufactured by Davison Co., Ltd., Sylopol 948, average particle size=55 μm, pore volume=1.66 ml / g, specific surface area=309 m) heat-treated at 300° C. with nitrogen flow 2 / g). 13 ml of toluene was added to obtain a slurry, and a solution of 0.668 g (2.04 mmol) of samarium (III) isopropoxide in 17 ml of toluene was slowly added dropwise. The mixture was stirred at room temperature for 2 hours, the supernatant liquid was removed by filtration, and the remaining solid compound was washed four times with 20 ml of toluene. Then, 30 ml of toluene was added to obtain a slurry, and 2.0 ml (4.0 mmol) of pentafluorophenol (2 mol / L, toluene solution) was slowly added. The mixture was stirred at 80°C for 2 hours, t...

Embodiment 2

[0159] (1) Preparation of modified particles

[0160] A 50 ml four-necked flask equipped with a stirrer, dropping funnel and thermometer was dried under reduced pressure, and then the air in the flask was replaced with nitrogen. 0.39 g (2.1 mmol) of bis(cyclopentadiene)manganese and 30 ml of toluene were added to the flask, and the mixture was stirred. 0.77 g of silica (manufactured by Davison Co., Ltd., Sylopol 948; average particle diameter=55 μm; pore volume=1.66 ml / g; specific surface area=309 m) was added 2 / g). The mixture was stirred at room temperature for 2 hours, the supernatant liquid was removed by filtration, and the remaining solid compound was washed four times with 20 ml of toluene. Then, 30 ml of toluene was added to obtain a slurry, and 1.1 ml (2.2 mmol) of pentafluorophenol (2 mol / L, toluene solution) was slowly added. The mixture was stirred at 80°C for 2 hours, and the supernatant was removed by filtration. The remaining solid compound was washed four ...

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Abstract

Modified particles (A) obtainable by contacting particles (a) with a metal compound (b) selected from compounds of the Group VI, VII and XIV metal elements and compounds of the lanthanide series, and then contacting the particles with a compound (c) having a functional group containing active hydrogen or a non-proton donative Lewis basic functional group, and an electron-withdrawing group; a carrier composed of the modified particles; a catalyst component for olefin polymerization composed of the modified particles; a catalyst for olefin polymerization obtainable by contacting the modified particles (A) and a transition metal compound (B), or further an organometallic compound (C); and a process for producing an olefin polymer with the catalyst.

Description

[0001] This application is a divisional application of the parent case with application number CN200410102007.0. The filing date of the parent case is December 25, 2000; the title of the invention is "modified particles and olefin polymerization catalysts and methods for producing olefin polymers using the same". technical field [0002] The present invention relates to particles suitable for use as a carrier and catalyst component for olefin polymerization, a catalyst for olefin polymerization using the particles, and a method for producing an olefin polymer using the catalyst for olefin polymerization. Background technique [0003] Olefin polymers such as polypropylene and polyethylene have been widely used in various molding fields due to their excellent mechanical and chemical resistance properties and a good balance between performance and economic benefits. These olefin polymers have hitherto been prepared by the polymerization of olefins, mainly using so-called Ziegle...

Claims

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Application Information

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IPC IPC(8): C09C1/00C09C3/06C08F4/02C08F210/02C08F4/42
Inventor 高冲和夫宫竹达也
Owner SUMITOMO CHEM CO LTD