Loaded metallocene catalyst and preparation method thereof

A technology of metallocene catalysts and metallocene compounds, applied in the field of supported metallocene catalysts and their preparation, to achieve high catalytic efficiency, low cost, and simple and easy preparation methods

Active Publication Date: 2012-05-16
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This patented new type of support for metallocene compounds that has improved activity compared with existing supports while reducing costs. It achieves this by supporting them on an organic material called Silgel instead of rods themselves. Additionally, its performance at both polymersizing (polymer)ethane/hexadecene and coating materials like poly(vinylidine chloride)) improves over previous methods due to increased surface area provided between these two types of molecules. Overall, this technology makes possible better ways to use these catalysts more efficiently than current alternatives without adding extra weight but still maintaining their effectiveness under specific conditions.

Problems solved by technology

This patents describes various methods for improving the properties of metallocene catalysis without increasing costs associated therewith. One approach involves carrying these catalyst particles onto carriages called molecular Sievers made of porous silica gel beforehand. These carriage particles help prevent degradations caused by small hydrocarbons while maintaining desired characteristics such as being able to load more efficiently and controllably within reactors like fluid bed processes. Another solution involve adding other types of moleculaeifiers between layers of the catalysator layer to enhance catalyst's ability to hold smaller molecules inside them. Additionally, introducing a special type of organic ligands called nitrogen atom donators could introduce functional sites through chemical bondings instead of physical binding.

Method used

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  • Loaded metallocene catalyst and preparation method thereof
  • Loaded metallocene catalyst and preparation method thereof
  • Loaded metallocene catalyst and preparation method thereof

Examples

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Embodiment 1

[0063] This example is used to illustrate the supported metallocene catalyst and its preparation method according to the present invention.

[0064] SBA-15 (commercially purchased from Jilin University High-Tech Co., Ltd., Changchun, Jilin) ​​and silica gel 955 (purchased from Shandong Lianke Silica Co., Ltd., with an average diameter of 20 microns and a specific surface area of ​​250m 2 / g) calcined at 400°C for 10 hours under the protection of nitrogen at a weight ratio of 1:2 to remove hydroxyl groups and residual moisture, thereby obtaining a carrier (named SBA-15-955-1);

[0065] Transfer 1.14 g of SBA-15-955-1 to a 250 ml glass reactor fully replaced by nitrogen, add 10 ml of refined toluene (refluxing with sodium for 24 hours before toluene is used) and 1.14 g of methylalumoxane ( commercially available from Albemarle, USA), and stirred at 50° C. for 4 hours. After the reaction was completed, let it stand, and filter out the liquid after the layers were separated, and w

experiment Embodiment 1

[0075] This experimental example is used to illustrate the catalytic efficiency of the supported metallocene catalyst according to the present invention.

[0076] In a 2-liter stainless steel autoclave, replace three times each with nitrogen and ethylene, then add 200 ml of hexane, raise the temperature of the kettle to 80 ° C, then add 800 ml of hexane, and add 2 ml of hexane with the addition of hexane 1 mol / liter triethylaluminum (TEA) hexane solution, then add 61 mg of SBA-15-955-BU-1, continue to feed ethylene to raise the pressure to 1.0MPa and maintain it at 1.0MPa, and react at 70°C 1 hour. Obtain 334 grams of polyethylene particle powder, the bulk density (BD) of this polyethylene particle powder is 0.336g / mL, melt index MI 2.16 = 0.069 g / 10 min. It is determined by calculation that the efficiency of the catalyst is 5475gPE / (gcat h) (ie, 1.06×10 8 g PE / (molZr h)).

experiment Embodiment 2

[0078] This experimental example is used to illustrate the catalytic efficiency of the supported metallocene catalyst according to the present invention.

[0079] In a 2-liter stainless steel autoclave, replace three times each with nitrogen and ethylene, then add 200 ml of hexane, raise the temperature of the kettle to 80 ° C, then add 800 ml of hexane, and add 2 ml of hexane with the addition of hexane 1 mol / L of triethylaluminum (commercially purchased from Zhejiang Freed Chemical Co., Ltd.) hexane solution and 10 mL of hexene, followed by adding 40.3 mg of SBA-15-955-BU-1, raising the ethylene pressure to 1.0 MPa was maintained at 1.0 MPa, and reacted at 70°C for 1 hour. Obtain 220 grams of polymkeric substance, the bulk density (BD) of this polymkeric substance is 0.306g / mL, melt index MI 2.16 = 0.405 g / 10 min. It was determined by calculation that the efficiency of the catalyst was 5459g PE / (gcat h) (ie, 1.06×10 8 gPE / (molZr h)).

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Abstract

The invention provides a loaded metallocene catalyst, which comprises a carrier, and a metallocene compound and alkylaluminoxane loaded on the carrier, wherein the carrier is a compound of silica gel and bar-shaped SBA-15; and the metallocene compound has a structure shown as a formula I. The invention further provides a method for preparing the loaded metallocene catalyst. The method comprises the following step of: under the protection of an inert gas, loading alkylaluminoxane and a metallocene compound on the carrier one by one. In the loaded metallocene catalyst according to the invention, the compound of the industrial silica gel and the bar-shaped SBA-15 is taken as the carrier, so that the cost of the catalyst is lowered remarkably. The loaded metallocene catalyst according to the invention displays high catalytic efficiency when used for catalyzing homopolymerization of olefins and copolymerization of the olefins.

Description

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Claims

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Application Information

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Owner CHINA PETROLEUM & CHEM CORP
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