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A preparation method and application of a catalyst for preparing polyolefin particles with high sphericity and low particle size

A high sphericity, polyolefin technology, applied in the field of olefin polymerization, can solve the problems of increased processing cost, unfavorable processing, damage to polymer chain integrity, etc., and achieves the effect of reducing bulk density, simple method and particle size.

Active Publication Date: 2017-07-21
INST OF CHEM CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although physical and mechanical pulverization can reduce the particle size of polyolefins, it will firstly increase the processing cost, and secondly, this method will damage the chain integrity of the polymer, which may be detrimental to subsequent processing.

Method used

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  • A preparation method and application of a catalyst for preparing polyolefin particles with high sphericity and low particle size

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preparation example Construction

[0045] As mentioned above, the present invention discloses a method for preparing a catalyst for preparing polyolefin particles with high sphericity and low particle size, which comprises the following steps:

[0046] (a) magnesium halide, alcohol compound, auxiliary agent, part of the internal electron donor and solvent are mixed to prepare mixture I;

[0047] (b) Add the above-mentioned mixture I into the reactor, preheat it to -30°C-30°C, and add the titanium compound dropwise; or,

[0048]Add a titanium compound into the reactor, preheat it to -30°C-30°C, and add the above-mentioned mixture I dropwise;

[0049] (c) After the dropwise addition is completed, the temperature of the reaction system is raised to 90°C-130°C after 30 minutes to 3 hours, and the remaining internal electron donor is added to continue the reaction;

[0050] (d) filter out the liquid in the reaction system, add the remaining titanium compound, and continue the reaction;

[0051] (e) After the react...

Embodiment 1

[0063] In the reactor fully replaced by high-purity nitrogen, add 4.94g of anhydrous magnesium chloride, 18.9g of isooctyl alcohol, and 30ml of decane in sequence, raise the temperature to 130°C under stirring, and maintain it for 2 hours, then add 2.65g of tetrabutyl titanate The ester and 2.05g of diisobutyl phthalate were reacted at 130°C for 1 hour, and finally cooled to room temperature to form a homogeneous transparent solution, namely mixture I.

[0064] Add 200ml of titanium tetrachloride to the reaction kettle, stir and preheat to 0°C, add the mixture I dropwise to the titanium tetrachloride in about 2 hours. After the dropwise addition was completed, the temperature was raised to 110° C. within 2 hours. 1.23 g of internal electron donor diisobutyl phthalate was added. After reacting at this temperature for 2 hours, remove the reaction liquid, add 200ml of titanium tetrachloride again, and react for 2 hours. Finally, the reaction liquid was removed, and the remainin...

Embodiment 2

[0067] In the reactor fully replaced by high-purity nitrogen, add 4.94g of anhydrous magnesium chloride, 18.9g of isooctyl alcohol, and 30ml of decane in sequence, raise the temperature to 130°C under stirring, and maintain it for 2 hours, then add 2.65g of tetrabutyl titanate The ester and 2.05g of diisobutyl phthalate were reacted at 130°C for 1 hour, and finally cooled to room temperature to form a homogeneous transparent solution, namely mixture I.

[0068] Add the mixture I to the reaction kettle, stir and preheat to 0°C, and add 100 mL of titanium tetrachloride dropwise into the reaction kettle for about 1 hour. After the dropwise addition was completed, the temperature was raised to 110° C. within 2 hours. 1.23 g of internal electron donor diisobutyl phthalate was added. After reacting at this temperature for 2 hours, remove the reaction liquid, add 200ml of titanium tetrachloride again, and react for 2 hours. Finally, the reaction liquid was removed, and the remainin...

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Abstract

The invention provides a preparing method of catalyst for preparation of high-spherical low-particle-size polyolefin particles. The catalyst is used for olefinic polymerization, the prepared polyolefin particles are of high sphericalness, small particle size (averagely 50 micrometers to 30 micrometers), narrow particle size distribution and low bulk density (0.1g / mL to 0.4g / mL). By means such as adjusting the forming temperature of a catalyst carrier and forming time of the catalyst and using any added nanoparticle as a third component for accelerating the formation of the catalyst, the catalyst is of small particle size and high sphericalness; according to replication of heterogeneous catalysts, submicron polyolefin spherical particles are prepared.

Description

technical field [0001] The invention relates to the technical field of olefin polymerization, in particular to a preparation method and application of a catalyst for preparing polyolefin particles. Background technique [0002] Ziegler-Natta catalyst is an organometallic catalyst for the synthesis of unbranched, highly stereoregular polyolefins, also known as Ziegler-Natta initiator, which belongs to coordination polymerization initiation agent. In 1956, German organic chemist Ziegler first discovered TiCl 4 / Et 3 The Al system can effectively catalyze the polymerization of ethylene at a lower pressure, and then the Italian chemist Natta developed this catalytic system for the isotactic polymerization of propylene, butadiene, isopentene, etc. These catalysts were later called homogeneous Geller-Natta catalyst. [0003] From the invention of the Ziegler-Natta catalyst in the 1950s to the present, the Ziegler-Natta catalyst has been continuously updated, from the first gen...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F110/06C08F4/649C08L23/12B29C67/24B33Y70/00
Inventor 李化毅罗志张辽云胡友良
Owner INST OF CHEM CHINESE ACAD OF SCI