A preparation method of a composite support for a propylene high temperature polymerization catalyst, a component of the propylene high temperature polymerization catalyst and the propylene high temperature polymerization catalyst

A technology of high-temperature polymerization and composite carrier, which is applied in the preparation of composite carrier for propylene high-temperature polymerization catalyst, components of propylene high-temperature polymerization catalyst and propylene high-temperature polymerization catalyst, and can solve problems such as difficult control of alcohol content, low isotacticity and complex process

Active Publication Date: 2019-11-19
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] Chinese patent CN 1524886A utilizes spray method to prepare MgCl 2 -SiO 2 Composite carrier, the composite carrier is made by contacting magnesium halide such as magnesium chloride with one or more electron donor compounds such as fatty alcohol, tetrahydrofuran, etc. to form a solution, which is mixed with silica gel with an average particle size of less than 30 μm, and spray-dried to obtain Spherical particles, the catalyst component and the cocatalyst component are used together for olefin polymerization, especially for propylene polymerization, showing high polymerization activity and stereospecificity, but the preparation of the carrier by spraying method needs to evaporate a large amount of Solvent, high energy and material consumption and the alcohol content of the obtained carrier is not easy to control
[0008] When the traditional Z-N catalyst is used for propylene polymerization, the polymerization temperature is generally below 80°C. When the polymerization temperature is higher than 80°C, the polymerization activity and the isotacticity and molecular weight of the prepared polymer will be greatly affected. The reason is that as the polymerization temperature increases, the deactivation of the active center of the catalyst is accelerated, resulting in a decrease in the polymerization activity of the system, an increase in the number of oligomers generated, and a low isotacticity of the final polymer.
[0009] For example, U.S. Patent No. 5,385,993 discloses a catalyst that can carry out propylene polymerization at a polymerization temperature of 150 to 300°C to obtain polypropylene with relatively high isotacticity. The propylene polymerization reaction has a wider molecular weight distribution, but at such a high polymerization temperature, the obtained polymer is no longer granular, and there will be problems such as difficult transportation in actual production.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] 1. Preparation of composite carrier

[0046] The silica gel carrier was first activated at 200°C for 1.5 hours, then the activation temperature was increased, and activated at 500°C for 4 hours; under nitrogen protection, 20.0 g of the activated silica carrier was added to 70 mL of toluene (toluene and silica The mass ratio of fluorene diether is 3:1), under stirring conditions, add 14.0g fluorene diether (the molar ratio of silicon dioxide and fluorene diether is 6:1), react at 15°C for 1 hour, evaporate the toluene solvent, and dry The treated silica gel carrier solid powder is obtained. Under the protection of nitrogen, 25.0 g of magnesium chloride and 42.9 mL of ethanol were added to the reactor (the molar ratio of ethanol to magnesium chloride was 2.8:1), and the temperature of the reactor was raised to 125 ° C until the magnesium chloride was completely melted.

[0047] Under the protection of nitrogen, add 5.0g of fluorene diether-treated silica gel carrier with...

Embodiment 2

[0053] 1. Preparation of composite carrier

[0054] Silica gel carrier pretreatment is the same as embodiment 1;

[0055] Under the protection of nitrogen, add 20.0g of magnesium chloride and 36.8mL of ethanol (the molar ratio of ethanol to magnesium chloride is 3.0:1) to the reactor, and raise the temperature of the reactor to 120°C until the magnesium chloride is completely melted.

[0056] Under the protection of nitrogen, add 5.0 g of the treated silica gel carrier with an average particle size of 20 μm to the reaction kettle for 30 minutes, and then add a mixed dispersant of 200 mL of liquid paraffin and 200 mL of methyl silicone oil preheated to 120 ° C into the reaction kettle to After stirring for 4 minutes at a speed of 800 rpm, the reaction mixture was transferred to a cooling kettle under the protection of nitrogen. The refrigerant in the cooling kettle was anhydrous hexane that had been precooled to -27°C in a sufficient amount. After stirring, cooling, MgCl is ob...

Embodiment 3

[0062] 1. Preparation of composite carrier

[0063] Silica gel carrier pretreatment is the same as embodiment 1;

[0064] Under nitrogen protection, add 20.0 g of magnesium chloride and 33.1 mL of ethanol (the molar ratio of ethanol to magnesium chloride is 2.7:1) to the reactor, and raise the temperature of the reactor to 115° C. until the magnesium chloride is completely melted.

[0065] Under the protection of nitrogen, add 10.0 g of the treated silica gel carrier with an average particle size of 20 μm to the reaction kettle for 30 minutes, then add the mixed dispersant of 200 mL of liquid paraffin and 200 mL of methyl silicone oil preheated to 115 ° C into the reaction kettle to After stirring for 4 minutes at a speed of 800 rpm, the reaction mixture was transferred to a cooling kettle under nitrogen protection. The refrigerant in the cooling kettle was anhydrous hexane that had been pre-cooled to -25°C in sufficient quantities. After stirring, cooling, MgCl is obtained a...

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Abstract

The invention relates to a preparation method of a composite support for a propylene high temperature polymerization catalyst, a component of the propylene high temperature polymerization catalyst andthe propylene high temperature polymerization catalyst. The composite support is prepared by a chemical reaction of a molten magnesium chloride alcohol adduct and a silica gel support treated by Lewis base. The composite support with good spherical shape and uniform particle distribution can be obtained by compounding a molten magnesium halide alcohol adduct with treated SiO2 through mechanical stirring. A titanium-containing catalyst and a cocatalyst prepared by the composite support exhibits excellent performance when used in olefin polymerization, especially in propylene polymerization athigh temperature (>=93 DEG C). The catalyst has high polymerization activity. An obtained high temperature polymer is good in particle form. Products have high bulk density and good stereoregularity.

Description

technical field [0001] The present invention relates to a magnesium chloride composite carrier and a propylene polymerization catalyst prepared therefrom. Specifically, magnesium chloride is compounded with silicon dioxide treated with a Lewis base to form a carrier and a catalyst solid component prepared from the carrier. The component When used in olefin polymerization, especially propylene high-temperature (≥93°C) polymerization, it shows excellent performance. The catalyst has high catalytic activity. The obtained high-temperature polymer particles have good shape, high bulk density and good stereoregularity. Background technique [0002] At present, the high-efficiency carrier-type Ziegler-Natta (Z-N) catalyst commonly used in olefin polymerization is to highly disperse the active components (such as Ti compounds) on the surface of the carrier, greatly increasing the specific surface area of ​​the catalyst, and significantly improving the catalytic efficiency of the cata...

Claims

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Application Information

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IPC IPC(8): C08F110/06C08F4/02C08F4/649
CPCC08F110/06C08F4/025C08F4/6494C08F2500/15
Inventor 宋赛楠曹庚振许云波刘强邓守军刘小燕张文学李丽董万卓张平生张翠玲钟赤锋刘文霞徐人威
Owner PETROCHINA CO LTD
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