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Supported single metallocene catalyst used for ethylene polymerization

A single metallocene and ethylene polymerization technology, which is applied in the field of preparation of modified silica gel supported single metallocene catalysts, can solve the problems of large amount of MAO, unusable, low activity, etc., and achieve high ethylene polymerization catalytic activity and good copolymerization reaction , the effect of simple preparation method

Active Publication Date: 2014-09-24
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Because the homogeneous single metallocene catalyst requires a large amount of MAO to achieve high activity, the production cost is high, and the obtained polymer is amorphous, which cannot be used in the widely used slurry method or gas phase polymerization process to overcome the above problems The most effective way is to support the soluble mono-metallocene catalyst
[0003] At present, there are a lot of research reports on the loading of single metallocenes, among which the catalysts using spherical magnesium chloride (containing alcohol) to support single metallocenes have good particle morphology, such as PCT Int.Appl.99 / 21898; US6,455,647; J.Mol .Catal.A2002,188,123; PCT Int.APP1.2004 / 078804, but the carrier contains alcohol, water, alkoxy and other components, and the preparation of the carrier is complicated; while Si0 2 CN1174849; CN1356343; US4,808,561; US5,026,797; US5,763,543; , a large amount of methylalumoxane must still be introduced during the polymerization process, the above shortcomings limit the industrial application of silica gel-supported single metallocene catalysts
There are also reports in the literature that a carrier containing magnesium chloride, silica gel, etc. is used to support a single metallocene (Polymer International, 51: 417-423, 2002; US5962360; CN102336855A), but the activity is very low, and a large amount of MAO needs to be added during polymerization
The above disadvantages limit the industrial application of silica-supported monometallocene catalysts

Method used

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  • Supported single metallocene catalyst used for ethylene polymerization

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0056] (1) Preparation of chlorinated hydrocarbyl silicon / silica gel support

[0057] Under the protection of nitrogen, take 10.0 grams of dry silica gel carrier and put it into a glass reactor, add 100 ml of dried hexane, disperse into a suspension, add 1 ml of SiCl 2 (n-Bu) 2 , start stirring, heat up to 30° C., react for 4 hours, and dry in vacuum to obtain a solid powder with good fluidity.

[0058] (2) Preparation of alkylmagnesium halide / hydrocarbyl silicon chloride / magnesium chloride carrier

[0059] Under the protection of nitrogen, take 10.0 grams of the above-mentioned modified silica gel carrier and add it to a glass reactor, add 100 ml of dried toluene, disperse it into a suspension, add 5 ml of 2M ethylmagnesium chloride, start stirring, heat up to 30 ° C, and react After 4 hours, it was vacuum dried to obtain a solid powder with good fluidity.

[0060] (3) Preparation of alkyl aluminoxane / hydrocarbyl magnesium halide / hydrocarbyl silicon chloride / magnesium chlo...

Embodiment 2

[0072] (1) Preparation of chlorinated hydrocarbyl silicon / silica gel support

[0073] With embodiment 1 step (1), only SiCl in embodiment 1 2 (n-Bu) 2 Change to SiCl 4 .

[0074] (2), (3), (4) are the same as the preparation methods of (2), (3), and (4) in Example 1.

[0075] The supported metallocene catalyst B was obtained. Characterized by ICP, in catalyst B, the weight content of Ti is 0.31%, the weight content of Al is 11.21%, and the weight content of magnesium is 2.67%.

Embodiment 3

[0077] (1) Preparation of chlorinated hydrocarbyl silicon / silica gel support

[0078] Same as step (1) of Example 1.

[0079] (2) Preparation of halogenated hydrocarbyl magnesium / chlorinated hydrocarbyl silicon / silica gel carrier

[0080] Same as step (2) of embodiment 1, only ethylmagnesium chloride in embodiment 1 is replaced by ethylmagnesium bromide.

[0081] (3), (4) are the same as in embodiment 1 (3), (4) preparation method

[0082] The supported metallocene catalyst C is obtained. Characterized by ICP, in catalyst C, the weight content of Ti is 0.29%, the weight content of Al is 10.87%, and the weight content of magnesium is 2.48%.

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Abstract

The invention relates to a supported single metallocene catalyst used for ethylene polymerization and a preparation method thereof. The catalyst comprises a single metallocene compound, a chlorinated alkyl silicon modifier, a halogenated alkyl magnesium modifier, alkyl aluminoxane and a silica gel carrier reaction product; the preparation method comprises the following steps: 1) preparation of a chlorinated hydroxyl silicon modified silica gel carrier, 2) preparation of a halogenated alkyl magnesium modified silica gel carrier, 3)preparation of an alkyl aluminoxane modified silica gel carrier, and 4)preparation of the silica gel supported single metallocene catalyst; and the obtained single metallocene catalyst has high polymerization activity for catalyzing vinyl polymerization or copolymerization. The preparation method of the silica gel carrier is simple, the obtained supported catalyst particles have good morphology and have adjustable size.

Description

technical field [0001] The invention relates to a preparation method of a modified silica gel supported mono-metallocene catalyst and the application of the obtained catalyst in olefin polymerization. technical background [0002] The development and application of a single metallocene catalyst is another major breakthrough in the field of olefin polymerization catalysts after the traditional Ziegler-Natta catalyst, especially in the 1980s, Kaminsky and Sinn et al. (Angew.Chem., 1980,19,390; Adv.Organoment .Chem., 1980,18,99) developed a high-efficiency cocatalyst methylaluminoxane (MAO), making the research on single metallocene catalysts enter a stage of rapid development. Because the homogeneous single metallocene catalyst requires a large amount of MAO to achieve high activity, the production cost is high, and the obtained polymer is amorphous, which cannot be used in the widely used slurry method or gas phase polymerization process to overcome the above problems The mo...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F10/02C08F4/6592
Inventor 高榕廖浩瀚李岩刘东兵周俊领黄廷杰
Owner CHINA PETROLEUM & CHEM CORP
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