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Olefin polymerization catalyst component as well as preparation method and catalyst thereof

A technology for olefin polymerization and catalysts, which is applied in the field of catalyst components for olefin polymerization and its preparation and catalysts. It can solve the problems of fast activity decay, complex production process, and insufficient activity in the later stage, and achieve slow activity decay, high catalytic activity, and production. low cost effect

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] The technology of forming the support in the above two ways to further prepare catalyst components has developed to a certain extent, mainly in the development of internal electron donors, such as diethers and succinates developed by BASELL, which are used to improve catalyst activity, Improve the hydrogen regulation performance of the catalyst, increase the molecular weight distribution of the product to improve the processing performance, but the increase in catalyst activity is mainly in the early stage of the polymerization reaction, and the activity decays quickly, so because the high activity in the early stage is not conducive to polymer production control, the production of copolymerization When using propylene, there are problems such as insufficient activity in the later stage, and the production process of this type of internal electron donor is generally complicated and the production cost is high, so the production cost of the catalyst is correspondingly high
[0005] Chinese patent CN1453298A discloses a class of glycol ester compounds containing a special structure 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, but the catalyst activity is limited. The improvement is also mainly in the early stage of the polymerization reaction, and the activity decays quickly. At the same time, the synthesis and purification process of this type of diol ester compound is complicated, which makes the catalyst production cost higher.
[0006] Generally speaking, there are many technologies to improve catalyst activity in the prior art, but the improvement of catalyst activity is usually accompanied by the acceleration of activity decay, which has a negative impact on the application of catalysts.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0031] 1. Preparation of titanium-containing solid catalyst components

[0032] In the reaction kettle that has been repeatedly replaced by high-purity nitrogen, add 4.8 grams of anhydrous magnesium chloride, 70 milliliters of toluene, 4.0 milliliters of epichlorohydrin, and 12.5 milliliters of tributyl phosphate, and react for 1 hour at a temperature of 60 ° C. , add 1.5 grams of phenol, 1.0 milliliters of benzoyl chloride and 30 milliliters of toluene, continue to react for one hour, cool down to -28°C, add 56 milliliters of titanium tetrachloride dropwise, gradually raise the temperature to 85°C, and add 1.1 milliliters of ortho Di-n-butyl phthalate (DNBP), keep the temperature for one hour, filter the mother liquor, wash twice with toluene, 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 washed 5 times with hexane, and the remaining solid product was vacuum-dried to obtain a ...

Embodiment 2

[0038] 1. Preparation of titanium-containing solid catalyst components

[0039] In the reaction kettle that has been repeatedly replaced by high-purity nitrogen, add 4.8 grams of anhydrous magnesium chloride, 70 milliliters of toluene, 4.0 milliliters of epichlorohydrin, and 12.5 milliliters of tributyl phosphate, and react for 1 hour at a temperature of 60 ° C. , add 1.5 grams of resorcinol, 2.0 milliliters of phthalic acid chloride and 35 milliliters of toluene, continue the reaction for one hour, cool down to -28°C, add 56 milliliters of titanium tetrachloride dropwise, gradually raise the temperature to 85°C, at 80°C Add 1.1 ml of di-n-butyl phthalate (DNBP), 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 hour, After filtration, the treatment was repeated twice, and then washed 5 times with hexane, and the remaining solid product w...

Embodiment 3

[0045] 1. Preparation of titanium-containing solid catalyst components

[0046] With embodiment 1, just phenol changes naphthol into. Among them, the titanium content is 4.6wt%, the DNBP content is 10.8wt%, the magnesium content is 17.8wt%, and the phosphorus content is 0.1wt%.

[0047] 2. Polymerization with a reaction time of 1 hour

[0048] With embodiment 1.

[0049] 3. Polymerization with a reaction time of 2 hours

[0050] 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 preparation method and application thereof. The catalyst component is prepared through the following steps: (1) enabling a magnesium compound, an organic epoxy compound and an organic phosphorus compound to be in contact with each other in a solvent to form a uniform solution; (2) with the existence of a mixed type assistant precipitation agent, 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 invention relates to a catalyst component for olefin polymerization or copolymerization, its preparation method, 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 obtain...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F10/00C08F4/649C08F4/654C08F4/651
Inventor 郭正阳王迎任春红王宇刘萃莲雷世龙洪挺付梅艳
Owner CHINA PETROLEUM & CHEM CORP