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Olefin polymerization catalyst and preparation method thereof and olefin polymerization method

A technology of olefin polymerization and catalyst, which is applied in the field of olefin polymerization, can solve the problems of high apparent density, high catalyst production cost, complex synthesis and purification process of diol ester compounds, etc., and achieve low production cost, high olefin polymerization activity, high The effect of catalytic activity

Inactive Publication Date: 2012-05-23
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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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] 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 resulting propylene polymer. The synthesis and purification process of the compound is complicated, which makes the catalyst production cost higher

Method used

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  • Olefin polymerization catalyst and preparation method thereof and olefin polymerization method

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preparation example Construction

[0019] The preparation method of the olefin polymerization catalyst of the present invention comprises: (1) contacting a magnesium compound, an organic epoxy compound, an organic phosphorus compound and an internal electron donor compound in a solvent to form a homogeneous solution; (2) in the presence of a precipitation aid , the homogeneous solution was contacted with a titanium compound to obtain a solid precipitate as the catalyst.

[0020] According to the present invention, although the purpose of the present invention can be achieved as long as the internal electron donor is introduced in step (1), the inventors found in the preparation process that by properly controlling the amount of the internal electron donor compound in step (1) , the activity of the synthesized catalyst can be higher, wherein, relative to each mole of magnesium element, the amount of the internal electron donor compound is preferably 0.005-15 moles, more preferably 0.06-10 moles.

[0021] The inv...

Embodiment 1

[0060] In the atmospheric pressure reactor that has been repeatedly replaced by high-purity nitrogen, add 4.8 grams of anhydrous magnesium chloride, 70 milliliters of toluene, 8.0 milliliters of epichlorohydrin, 12.5 milliliters of tributyl phosphate, and 0.5 milliliters of di-n-butyl phthalate (DNBP), at a temperature of 50°C, reacted for 2 hours, added 1.4 grams of phthalic anhydride and 55 milliliters of toluene, reacted for one hour, cooled to -28°C, added dropwise 56 milliliters of titanium tetrachloride (drop acceleration 5 ml / min), the temperature was raised to 85°C (the heating rate was 5°C / min), 0.6 ml of di-n-butyl phthalate (DNBP) was added, the temperature was maintained for one hour, filtered, the solid was washed twice with toluene, and then Add 48 ml of titanium tetrachloride and 72 ml of toluene, keep the temperature at 110°C for 0.5 hours, add 48 ml of titanium tetrachloride and 72 ml of toluene after filtering, and treat it once at 110°C for 0.5 hours, then tr...

experiment Embodiment 1

[0062] After 5 liters of stainless steel autoclaves were fully replaced with nitrogen, 5 milliliters of concentrations were added to be a hexane solution of 0.5 mol / liter of triethylaluminum and 1 milliliter of concentrations to be 1 mol / liter of methylcyclohexyldimethoxysilane ( CMMS) hexane solution and 10 mg of catalyst prepared in Example 1, then add 10 milliliters of hexane to flush the feed line, then add 1 liter (under standard state) hydrogen, and 2 liters of refined propylene, and heat up to 70 ° C. Polymerization was carried out at temperature for 1 hour. After the reaction, the temperature of the reactor was lowered and the stirring was stopped to discharge the reaction product to obtain an olefin polymer. See Table 1 for details of the results.

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Abstract

The invention provides an olefin polymerization catalyst and a preparation method thereof. The method comprises the following steps of: (1) enabling a magnesium compound, an organic epoxy compound, an organic phosphorus compound and an internal donor compound to contact in a solvent to form a uniform solution; and (2) enabling the uniform solution to contact with a titanium compound in the presence of an assistant precipitation agent to obtain a solid precipitate serving as the catalyst. The invention provides an olefin polymerization method. According to the method for preparing the olefin polymerization catalyst, an internal donor is introduced in the contacting process of the magnesium compound, the organic epoxy compound and the organic phosphorus compound in the solvent, so that the obtained catalyst has much higher activity than a catalyst obtained by loading the internal dolor onto a solid precipitate containing magnesium and titanium, obtained by adopting an assistant precipitation agent, in the prior art, and the catalytic activity of the catalyst for olefin polymerization is 1.1-1.5 times higher than that of a catalyst in the prior art.

Description

technical field [0001] The invention relates to a method for preparing an olefin polymerization catalyst, an olefin polymerization catalyst obtained by the method, and a method for olefin polymerization using the olefin polymerization catalyst. 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 m...

Claims

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Application Information

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IPC IPC(8): C08F10/00C08F4/654C08F4/651C08F4/649C08F4/645C08F4/646C08F10/02
Inventor 郭正阳任春红王迎王宇刘萃莲洪挺雷世龙付梅艳
Owner CHINA PETROLEUM & CHEM CORP
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