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Supported metallocene catalyst and its preparation method

A metallocene catalyst and metallocene compound technology, applied in the field of supported metallocene catalyst and its preparation, can solve the problems of low mechanical strength, high cost and low catalytic activity of mesoporous materials, and achieve stable structure, high catalytic activity, High catalytic activity

Active Publication Date: 2014-02-05
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0016] The object of the present invention is to overcome the problems of low catalytic activity, high cost and low mechanical strength of mesoporous materials of the supported metallocene catalysts of the prior art, and provide a supported metallocene catalyst with low cost, stable structure and high catalytic activity. metallocene catalyst

Method used

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  • Supported metallocene catalyst and its preparation method
  • Supported metallocene catalyst and its preparation method
  • Supported metallocene catalyst and its preparation method

Examples

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preparation example 1

[0078] This preparation example is used to illustrate the supported metallocene catalyst and its preparation method according to the present invention.

[0079] 1.5 gram of cetyltrimethylammonium bromide (CTAB) and 1.5ml density are 1.07g / ml, the polyethylene glycol octyl phenyl ether (triton X-100) of concentration weight 5% joins in In the hydrochloric acid solution that is the concentrated hydrochloric acid of 37% by weight and 75 grams of water by 29.6 gram concentration, stir until CTAB and Triton X-100 dissolve completely at 40 ℃; Add 4.6 grams of industrial sodium silicate to the above solution Stirring at 40°C for 15 minutes, the sodium silicate was completely dissolved, and then crystallized at 40°C for 24 hours, and the original powder mesoporous material was obtained after filtration, washing and drying; the original powder mesoporous material was heated in a muffle furnace at 600°C After calcination for 24 hours, the template agent was removed to obtain a spherical...

experiment Embodiment 1

[0093] This experimental example is used to illustrate the catalytic activity of the supported metallocene catalyst according to the present invention.

[0094] 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 The concentration is 1 mol / liter triethylaluminum (TEA) hexane solution, then add 62.3 milligrams of supported metallocene catalysts JKQ-YIN that above-mentioned embodiment 1 makes, feed ethylene and pressure is raised to 1.0MPa and maintain 1.0 MPa, react at 70°C for 1 hour. Obtain 100 grams of polyethylene particle powder, the bulk density (BD) of this polyethylene particle powder is 0.300g / ml, melt index MI 2.16 = 0.005 g / 10 min. It is determined by calculation that the efficiency of the catalyst is 1605g PE / (gcat h) (ie, 4.2×10 7 gPE / (mol Zr h)).

experiment Embodiment 2

[0096] This experimental example is used to illustrate the catalytic activity of the supported metallocene catalyst according to the present invention.

[0097] 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 70 ° C, then add 800 ml of hexane, and add 2 ml of hexane with the addition of hexane The concentration of 1 mol / liter of triethylaluminum (TEA) hexane solution and 10 milliliters of hexene, then add the supported metallocene catalyst JKQ-YIN that 64.4 milligrams above-mentioned embodiment 1 makes, feed ethylene to reduce the pressure Raise to 1.0MPa and maintain at 1.0MPa, react at 70°C for 1 hour. Obtain 47 grams of polymkeric substance, the bulk density (BD) of this polymkeric substance is 0.290g / ml, melt index MI 2.16 = 0.200 g / 10 min. It was determined by calculation that the efficiency of the catalyst was 730g PE / (gcat h) (ie, 1.9×10 7 g PE / (molZr h)).

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Abstract

The invention discloses a supported metallocene catalyst and its preparation method, and is characterized in that the catalyst comprises a carrier and a metallocene compound and alkyl aluminoxane which are loaded on the carrier. The carrier is spherical mesoporous silicon dioxide. The average particle diameter of the carrier is 1-10 micrometers, its specific surface area is 1000-2000 square meter / gram, its pore volume is 0.3-1.5 ml / g, and its most probable pore size is 4-20 nanometers. The metallocene compound has a structure as shown in the formula 1 defined in the specification, in which M is one of titanium, zirconium and hafnium and X is halogen. When the supported metallocene catalyst provided by the invention is used to catalyze alkene polymerization, the catalytic efficiency can reach 1605g PE / gcath.

Description

technical field [0001] The invention relates to a supported metallocene catalyst and a preparation method thereof. Background technique [0002] The development and application of metallocene catalysts is another major breakthrough in the field of olefin polymerization catalysts after the traditional Ziegler-Natta catalysts. Due to the large amount of methylaluminoxane (MAO) required to achieve high activity of homogeneous metallocene catalysts, the production cost is high, and the obtained polymer has no particle shape, it cannot be used in the widely used slurry method or gas phase polymerization process. use. Moreover, the activity of the metallocene catalyst is very high, and it is prone to localized polymerization at a faster rate during the polymerization reaction, which in turn leads to detonation. [0003] An effective way to solve the above problems is to carry out loading treatment on soluble metallocene catalysts. At present, in the research reports on metalloc...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F4/6592C08F4/02C08F10/00
Inventor 亢宇张明森王洪涛邱波郭顺刘长城
Owner CHINA PETROLEUM & CHEM CORP