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Magnesium halide carrier and application thereof, and olefin polymerization catalyst, olefin polymerization catalyst system, and olefin polymerization method

A technology of olefin polymerization and magnesium halide, applied in olefin polymerization catalysts and olefin polymerization catalyst systems, in the field of olefin polymerization, to achieve the effects of increased production capacity, low production cost, and strong load capacity

Active Publication Date: 2015-04-29
CHINA PETROLEUM & CHEM CORP +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In addition, the active center content of the Ziegler-Natta type catalyst prepared with the existing active magnesium chloride as a carrier needs to be further improved

Method used

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  • Magnesium halide carrier and application thereof, and olefin polymerization catalyst, olefin polymerization catalyst system, and olefin polymerization method

Examples

Experimental program
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preparation example Construction

[0020] The preparation method of the magnesium halide carrier according to the present invention may comprise, in the presence of a seed crystal, contacting metallic magnesium with a halogenated alkane represented by formula I to form a magnesium halide,

[0021] R 1 x 1 (Formula I),

[0022] In formula I, R 1 for C 3 -C 12 straight-chain or branched-chain alkyl, X 1 is halogen (for example: fluorine, chlorine, bromine or iodine).

[0023] According to the present invention, in formula I, R 1 preferably C 3 -C 6 Alkyl; X 1 It is preferably chlorine, bromine or iodine, more preferably chlorine or bromine, still more preferably chlorine.

[0024] In the present invention, the C 3 -C 12 Examples of linear or branched alkyl groups can be, but are not limited to: n-propyl, isopropyl, n-butyl, sec-butyl, isobutyl, tert-butyl, n-pentyl, isopentyl, tert-amyl Nyl, neopentyl, n-hexyl, n-heptyl, n-octyl, n-decyl and n-dodecyl.

[0025] According to the present inven...

Embodiment 1

[0060] (1) Preparation of magnesium halide carrier

[0061] In a 500mL five-neck reaction flask equipped with a stirrer, condenser, dropping funnel and heating device, add 150mL of n-hexane, 1.5g of magnesium powder and 6g of clay (commercially purchased from Zhejiang Fenghong Clay Chemical Co., Ltd., average particle 40 microns in diameter, dried at a temperature of 200°C for 4 hours before use), 14mL of n-chlorobutane was added dropwise to the reaction flask at a temperature of 60°C, and the dropping time was 2 hours. After the dropwise addition was completed, The reaction was continued for 2 hours at a temperature of 60°C. After the reaction was completed, the reaction mixture was cooled to room temperature, filtered, and washed 3 times with n-hexane to obtain 100 mL of a suspension containing the magnesium halide carrier according to the present invention (wherein the concentration of the magnesium halide carrier was 0.055 g / mL). Based on the total amount of the magnesium...

Embodiment 2

[0068] (1) Preparation of magnesium halide carrier

[0069] In a 500mL five-neck reaction flask equipped with a stirrer, condenser, dropping funnel and heating device, add 150mL of n-hexane, 1.5g of magnesium powder and 6g of montmorillonite (commercially purchased from Zhejiang Fenghong Clay Chemical Co., Ltd., The average particle diameter is 25 microns, dried at a temperature of 200°C for 4 hours before use), and 14 mL of n-chlorobutane was added dropwise to the reaction flask at a temperature of 60°C, and the addition time was 2 hours, and the addition was completed After that, the reaction was continued for 3 hours at a temperature of 60°C. After the reaction was completed, the reaction mixture was cooled to room temperature, filtered, and washed 3 times with n-hexane to obtain 100 mL of a suspension containing the magnesium halide carrier according to the present invention (wherein the concentration of the magnesium halide carrier was 0.052 g / mL). Based on the total amo...

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Abstract

The invention provides a magnesium halide carrier and an application thereof, and an olefin polymerization catalyst, an olefin polymerization catalyst system, and an olefin polymerization method. The magnesium halide carrier provided by the invention comprises magnesium halide and crystal seed, wherein the crystal seed is one or more selected from montmorillonite, clay, kaolin, diatomite, bentonite, argil and alumina. The magnesium halide carrier provided by the invention has a high loading capacity, such that high active component load can be obtained. With the magnesium halide carrier provided by the invention, prepared olefin polymerization catalyst has high catalytic activity. When the catalyst is used in olefin polymerization, prepared polyolefin product has high bulk density. Also, the magnesium halide carrier provided by the invention has simple preparation process and low production cost.

Description

technical field [0001] The invention relates to a magnesium halide carrier and application thereof, and also relates to an olefin polymerization catalyst and an olefin polymerization catalyst system, and further relates to an olefin polymerization method. Background technique [0002] Traditional Ziegler-Natta type catalysts include a main catalyst and a cocatalyst, the main catalyst is usually a compound containing the metal elements of Group IVB in the periodic table, the most commonly used is a titanium compound; the cocatalyst is usually an organoaluminum compound, Common cocatalysts include Al(C 2 h 5 ) 3 , Al(C 2 h 5 ) 2 Cl, Al 2 (C 2 h 5 ) 3 Cl 3 Wait. [0003] The performance of Ziegler-Natta catalysts used in the synthesis of polyethylene has been greatly improved after several generations of development, and the birth of supported catalysts has significantly improved the polymerization activity of Ziegler-Natta catalysts. Activated magnesium chloride is...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F4/02C08F4/645C08F10/00C08F10/02
Inventor 肖明威郭宇李阳阳叶晓峰
Owner CHINA PETROLEUM & CHEM CORP