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Catalyst component, preparation method and catalyst for olefin polymerization

An olefin polymerization and catalyst technology, which is applied in the field of solid catalyst components, can solve the problems of difficult preparation, low preparation yield and low activity, and achieves the effects of mild and simple synthesis conditions, reduced production costs, and high sensitivity to hydrogen adjustment.

Active Publication Date: 2021-09-21
BEIJING LIHE TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] However, in practical applications, there are certain problems in the above-mentioned compounds as internal electron donors of catalysts for olefin polymerization. The relative molecular mass distribution of polypropylene is relatively narrow, and phthalate compounds are commonly used as plasticizers, which are very harmful to human reproductive health and the environment; 1,3-diether compounds are used as internal plasticizers. Although the electron donor catalyst has high activity and good hydrogen modulation sensitivity, the relative molecular weight distribution of the prepared PP is narrow, which is not conducive to the development of different brands of PP; succinate compounds are used as internal electron donors. The advantage is that the relative molecular mass distribution of the synthesized PP is relatively wide. The disadvantage is that the stereoregularity of PP and the hydrogenation sensitivity of the catalyst need to be improved, and the overall activity of the diol lipid catalytic system is not as ideal as that of the diether system.
[0005] 1,3-diether compounds need to be prepared through a two-step reaction, the production process is longer, and the production yield of succinate compounds is low, while the main raw materials of diol ester compounds such as 2,4-pentanediol are difficult The preparation leads to higher prices, so the production costs of the above-mentioned electron donor compounds are all higher, which is not conducive to the marketing of products

Method used

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  • Catalyst component, preparation method and catalyst for olefin polymerization
  • Catalyst component, preparation method and catalyst for olefin polymerization
  • Catalyst component, preparation method and catalyst for olefin polymerization

Examples

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preparation example Construction

[0100] Preparation of solid catalyst components

[0101] The operations for preparing catalysts / catalyst components in the following examples / comparative examples were all carried out under the protection of high-purity nitrogen. details as follows:

Embodiment 1

[0103] In a 500ml stirred 5-neck flask fully replaced by nitrogen, add 10g of diethoxymagnesium and 80mL of toluene to prepare a suspension, and then add 20mL of titanium tetrachloride dropwise at -10°C. After the dropwise addition, the system After slowly raising the temperature to 10°C, add 60mL of titanium tetrachloride dropwise, then slowly raise the temperature to 90°C, add 2.5g of 1,1'oxy-bis-2-propanol-dibenzoate, and then continue to heat up to 120°C Keep the temperature constant for 2 hours, then press filter the liquid, remove the liquid, and wash the obtained solid three times with 120 mL of titanium tetrachloride at 125°C. The obtained solid was washed twice with 150 mL of hexane at 60°C and twice at room temperature, and the liquid was filtered off and dried to obtain 9.86 g of solid powder which was the solid catalyst component. Table 2 shows the titanium content, internal electron donor content and polymerization data of the solid catalyst component.

Embodiment 2-24

[0105] The preparation process of the solid catalyst component is as shown in Example 1, except that 1,1'oxy-bis-2-propanol-dibenzoate is replaced by the compounds in Table 1 in sequence.

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Abstract

The invention discloses a catalyst component for olefin polymerization, which comprises Mg, Ti, halogen and an electron donor compound, wherein: the electron donor compound includes at least one compound selected from the general formula (I) The first electron donor compound of ester ether compound. The invention also discloses a preparation method of the catalyst component and a catalyst for olefin polymerization containing the catalyst component. The invention adopts the diacid ether compound as the catalyst of the internal electron donor, has excellent activity and good stereospecificity, and the molecular weight distribution of the obtained polymer is relatively wide. Moreover, the catalyst also has high hydrogen adjustment sensitivity, which can be adjusted by adjusting the hydrogen partial pressure [p(H 2 )] to adjust the relative molecular mass of polyolefins to achieve the purpose of controlling their melt flow rate, and the "hydrogen adjustment method" can be used to directly prepare polyolefins with high melt flow rates.

Description

technical field [0001] The present invention relates to a method for CH 2 =CHR Catalyst component for olefin polymerization, more particularly, the present invention relates to a solid catalyst component containing at least one specific type of diacid ether compound. In addition, the present invention also relates to a catalyst containing the solid catalyst component and the application of the catalyst in olefin polymerization. Background technique [0002] In the propylene polymerization industry, the most widely studied and applied catalyst is the Ziegler-Nata catalyst, which is prepared by adding an internal electron donor during the process of loading titanium on an active magnesium chloride carrier. Since the internal electron donor can change the catalyst performance to the greatest extent, the research and search for the ideal internal electron donor compound has become the focus and hotspot of Ziegler-Nata catalyst research. At present, research on internal electro...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F10/00C08F110/06C08F4/649C08F4/646
CPCC08F10/00C08F110/06C08F4/6494C08F4/6495C08F4/6465C08F2500/15C08F2500/04
Inventor 王志武李树行李华姝张军伟代金松马庆利胡乐陈灏王星火焦文杰高勇
Owner BEIJING LIHE TECH