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Carrier for olefin polymerization catalyst, olefin polymerization catalyst and process for producing olefin polymer

A catalyst carrier, a technology for olefin polymerization, which is applied in the field of olefin polymerization catalyst carrier and olefin polymerization catalyst to prepare olefin polymer, and can solve the problems of catalyst composition not being released from the carrier and limiting the use of solvents, etc.

Inactive Publication Date: 2002-12-11
SUMITOMO CHEM CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, since there is no chemical bond between the catalyst composition and the support in the supported catalysts disclosed in these publications, there is a problem that the use of solvents is limited in the polymerization reaction and the preparation of the catalyst, so that the catalyst composition does not Issues such as release from the carrier

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0050] (1) Preparation of organic polymer carrier

[0051] In a 2-liter Erlenmeyer flask equipped with a stirrer, a reflux condenser and a thermometer, 60 grams of acrylonitrile-divinylbenzene copolymers (the content of divinylbenzene units are 10% by weight) The micropore capacity of 5000A micropores is 0.62ml / g, the radius is 35-50,000A micropores have a micropore capacity of 0.71ml / g, and the average particle size is 50μm). And add 206 grams of diethylenetriamine and 36 grams of distilled water, react at 130-140° C. for 4 hours, filter the supernatant, and wash the obtained solid twice with 1 liter of distilled water. Dry in vacuo to a flowable solid (158 g).

[0052] The obtained olefin polymerization catalyst support had a pore volume of 0.46 ml / g for pores with a pore radius of 100-5,000 Å, a pore volume of 0.48 ml / g for pores with a pore radius of 35-50,000 Å, and an average particle size of 45 μm.

[0053] (2) Preparation of solid catalyst composition

[0054] Air i...

Embodiment 2

[0060] (1) Preparation of olefin polymerization catalyst carrier

[0061] In a 2-liter Erlenmeyer flask equipped with a stirrer, a reflux condenser and a thermometer, 71.1 grams of acrylonitrile-divinyl copolymer (the content of divinylbenzene units is 10% by weight, and the radius is 100-5,000 The micropore volume of A micropore is 0.62ml / g, and the radius is 35-50,000A micropore volume is 0.71ml / g, and the average particle diameter is 50 μ m), add 356 grams of diethylamine and 78.9 grams of distilled water, in The reaction was carried out at 130°C for 7.5 hours, the supernatant was collected by filtration, and the obtained solid was washed twice with 1 liter of distilled water. Dry in vacuo to a flowable solid (36.3 g).

[0062] The obtained olefin polymerization catalyst support had a pore volume of 1.31 ml / g for pores with a pore radius of 100-5,000 Å, a pore volume of 1.56 ml / g for pores with a pore radius of 35-50,000 Å, and an average particle diameter of 40 μm.

[00...

Embodiment 3

[0070] (1) Preparation of olefin polymerization catalyst carrier

[0071] 71.1 grams of acrylonitrile-divinylbenzene copolymer (the content of divinylbenzene unit is 10% by weight) and the radius of 100- The micropore capacity of 5000A micropore is 0.62ml / g, and the radius is 35-50, the micropore capacity of 000A micropore is 0.71ml / g, and the average particle diameter is 50 μ m), add 447 grams of propylene diamine and 78.9 grams of distilled water, After reacting at 130°C for 7.5 hours, the supernatant was collected by filtration, and the obtained solid was washed twice with 1 liter of distilled water. Dry in vacuo to a flowable solid (42 g).

[0072] The obtained olefin polymerization catalyst carrier had pores with a micropore volume of 0.54 ml / g for micropores with a pore radius of 100-5,000 Å, and pores with a micropore capacity of 0.64 ml / g for micropores with a radius of 35-50,000 Å, average The particle size is 45 μm.

[0073] (2) Preparation of solid catalyst compo...

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Abstract

The present invention provides a porous acrylic acid polymer with polar functional groups, a solid catalyst composition for olefin polymerization obtained by loading a transition metal compound, and an organic aluminum compound and / or an organic aluminum oxyhydrogenation olefin polymerization catalyst carrier on the carrier; An olefin polymerization catalyst; and a method for preparing olefin polymers using the catalyst. The present invention provides olefin polymerization catalysts having high polymerization activity which, when used in slurry polymerization or gas phase polymerization, yield olefin polymers with excellent particle properties.

Description

technical field [0001] The present invention relates to an olefin polymerization catalyst support and a method for preparing olefin polymers using the olefin polymerization catalyst supported. Specifically, the present invention relates to an olefin polymerization catalyst support suitable for slurry polymerization or gas phase polymerization, having high polymerization reactivity and imparting excellent particle characteristics to olefin polymers, and a method for producing olefin polymers using the olefin polymerization catalyst supported . Background technique [0002] There have been many reports on the production of olefin polymers using olefin polymerization catalysts of transition metal compounds. For example, in the case of metallocene transition metal compounds, the preparation of olefin polymers using metallocene catalysts and alumoxanes is disclosed in USP 4,542,199. In JP-A-01-502036 (1989), there is also disclosed a method for producing an...

Claims

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Application Information

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IPC IPC(8): C08F4/00C08F4/02C08F4/60C08F4/642C08F4/6592C08F10/00
CPCC08F4/027C08F10/00C08F4/61916C08F4/02C08F4/64
Inventor 熊本伸一白石宽之今井昭夫
Owner SUMITOMO CHEM CO LTD