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Olefin polymerization catalyst component as well as catalyst and application thereof

A technology for olefin polymerization and catalyst, which is applied to catalyst components for olefin polymerization, catalysts and application fields, can solve the problems of complex synthesis and purification process of glycol ester compounds, high catalyst production cost, low catalyst activity and the like, and achieves activity attenuation The effect of slow, low production cost and easy availability of raw materials

Active Publication Date: 2015-04-29
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

When the catalyst system is used for propylene polymerization, the obtained polymer has high isotacticity and high apparent density, but the catalyst activity is not high
[0004] Chinese patent CN1453298A discloses a class of glycol ester compounds containing special structures as electron donors. The use of such electron donors can not only improve the activity of the catalyst, but also significantly broaden the molecular weight distribution of the obtained propylene polymer. The synthesis and purification process of alcohol ester compound is complicated, which makes the catalyst production cost higher

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] 1. Preparation of titanium-containing solid catalyst components

[0031] In the reaction kettle repeatedly replaced by high-purity nitrogen, 4.8 grams of anhydrous magnesium chloride, 70 milliliters of toluene, 4.0 milliliters of epichlorohydrin, 12.5 milliliters of tributyl phosphate and 1.0 milliliters of tetraethoxysilane were added successively, at a temperature of 60 Under the condition of ℃, react for 1 hour, add 1.5 grams of phenol, 1.0 milliliter of benzoyl chloride and 30 milliliters of toluene, continue to react for one hour, cool down to -28 ℃, dropwise add 56 milliliters of titanium tetrachloride, and gradually heat up to 85 ℃, Add 1.1 ml of di-n-butyl phthalate (DNBP) at 80°C, keep the temperature for one hour, filter off the mother liquor, wash twice with toluene, then add 48 ml of titanium tetrachloride and 72 ml of toluene, keep the temperature at 110°C After 0.5 hour, filter and repeat the treatment twice, then wash with hexane for 5 times, and vacuum d...

Embodiment 2

[0037] 1. Preparation of titanium-containing solid catalyst components

[0038] In the reaction kettle repeatedly replaced by high-purity nitrogen, 4.8 grams of anhydrous magnesium chloride, 70 milliliters of toluene, 4.0 milliliters of epichlorohydrin, 12.5 milliliters of tributyl phosphate and 2.0 milliliters of tetraethoxysilane were added successively, at a temperature of 60 Under the condition of ℃, react for 1 hour, add 1.5 grams of resorcinol, 2.0 milliliters of benzoyl chloride and 35 milliliters of toluene, continue to react for one hour, cool down to -28 ℃, add dropwise 56 milliliters of titanium tetrachloride, and gradually heat up to 85°C, add 1.1 ml of di-n-butyl phthalate (DNBP) at 80°C, keep the temperature for one hour, filter off the mother liquor, wash twice with toluene, then add 48 ml of titanium tetrachloride and 72 ml of toluene. Keep the temperature at 110°C for 0.5 hours, filter and repeat the treatment twice, then wash with hexane for 5 times, and vacu...

Embodiment 3

[0044] 1. Preparation of titanium-containing solid catalyst components

[0045] With embodiment 1, just phenol changes naphthol into. The content of titanium in the catalyst is 4.3wt%, the content of DNBP is 10.6wt%, the content of magnesium is 18.1wt%, the content of phosphorus is 0.1wt%, and the content of silicon is 0.1wt%.

[0046] 2. Polymerization with a reaction time of 1 hour

[0047] With embodiment 1.

[0048] 3. Polymerization with a reaction time of 2 hours

[0049] With embodiment 1.

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PUM

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Abstract

The invention discloses an olefin polymerization or copolymerization catalyst component as well as a catalyst and application thereof. The catalyst component is prepared through the following steps: (1) enabling a magnesium compound, an organic epoxy compound, an organic phosphorus compound and a silane compound to be in contact with each other in a solvent to form a uniform solution; (2) with the existence of a phenolic compound and an acyl chloride compound, enabling the uniform solution and a titanium compound to be in contact with each other to obtain a mixture; (3) enabling the mixture obtained in the step (2) and an electron donor compound to be in contact with each other, and obtaining the olefin polymerization titaniferous catalyst component through filtering, washing and drying. The olefin polymerization or copolymerization catalyst component has high catalytic activity and slow activity attenuation when being applied to propylene polymerization and copolymerization.

Description

technical field [0001] The present invention relates to a catalyst component for olefin polymerization or copolymerization, its catalyst, and its application in olefin polymerization or copolymerization. Background technique [0002] In the late 1970s, companies such as Mitsui Petrochemical Corporation of Japan and Monai of the United States successfully developed titanium-magnesium high-efficiency carrier catalysts with magnesium chloride as the carrier. Because the carrier was used to improve the utilization rate of the active center of the titanium atom, the catalytic activity was improved. It is much higher than conventional catalysts and simplifies the polymerization process, so the world's polyolefin industry has developed rapidly. Conventional methods for preparing highly active supported catalysts are generally co-grinding, grinding and impregnating, spraying carrier forming and high-speed stirring carrier forming, etc. The main disadvantage of the catalyst obtained...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F10/00C08F4/649C08F4/658C08F4/651
Inventor 郭正阳任春红王迎王宇刘萃莲雷世龙洪挺付梅艳
Owner CHINA PETROLEUM & CHEM CORP