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Olefin polymerization catalyst component and olefin polymerization catalyst and their use and olefin polymerization method

A technology for olefin polymerization and catalysts, applied in the field of olefin catalysts, can solve the problems of low ethylene structural unit content, low polymer bulk density, unstable preparation process, etc., and achieve the effect of increasing content and high activity

Active Publication Date: 2020-06-09
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the preparation of catalyst supports by this method has the disadvantages of unstable preparation process, easy formation of a large number of special-shaped particles, resulting in carrier adhesion of the carrier, and poor carrier molding effect. The bulk density of the polymer is also low, and the content of ethylene structural units is also low when used for copolymerization

Method used

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  • Olefin polymerization catalyst component and olefin polymerization catalyst and their use and olefin polymerization method
  • Olefin polymerization catalyst component and olefin polymerization catalyst and their use and olefin polymerization method
  • Olefin polymerization catalyst component and olefin polymerization catalyst and their use and olefin polymerization method

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Experimental program
Comparison scheme
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Embodiment approach

[0044] According to a preferred embodiment of the present invention, the average particle diameter of the olefin polymerization catalyst support can be 10-100 microns, preferably 40-60 microns, and the particle size distribution is less than 1.2, preferably 0.6-0.8. In this preferred embodiment, the catalyst prepared from the olefin polymerization catalyst support can obtain an olefin polymer having a higher bulk density. In the present invention, the average particle diameter and particle size distribution of the olefin polymerization catalyst carrier can be measured with a Master Sizer 2000 laser particle size analyzer (manufactured by Malvern Instruments Ltd).

[0045] According to the present invention, the olefin polymerization catalyst carrier may also carry a trace amount of water, which comes from the trace amount of water carried by the synthesis raw material and the reaction medium.

[0046] According to the present invention, the synthetic raw materials of the catalyst c...

preparation example 1

[0098] This preparation example is used to illustrate the olefin polymerization catalyst support provided by the present invention and the preparation method thereof.

[0099] In a 0.6L reaction kettle, 8.0g (0.08mol) magnesium chloride, 56mL (0.96mol) ethanol, and 4.3g (0.016mol) chromium trichloride hexahydrate were added, and the temperature was raised to 90°C under stirring. Constant temperature reaction for 2 hours. The mixture was stirred at low speed (400 revolutions per minute) and dispersed for 30 minutes to emulsify. And 0.48 mol (38 ml) of epichlorohydrin was added to the emulsified product, and after reacting for half an hour, it was filtered under pressure. The filtered product was washed 5 times with hexane and dried under vacuum to obtain a catalyst carrier Z1 for olefin polymerization.

[0100] Characterized by nuclear magnetic resonance and elemental analysis, the structure of the catalyst carrier Z1 obtained is as follows:

[0101]

[0102] The average particle di...

preparation example 2

[0104] This preparation example is used to illustrate the olefin polymerization catalyst support provided by the present invention and the preparation method thereof.

[0105] In a 1.6L reactor, add 300mL white oil, 8.0g (0.08mol) magnesium chloride, 28mL (0.48mol) ethanol, 2.1g (0.008mol) chromium trichloride hexahydrate, and heat up to 100°C with stirring. React for 0.5 hour. The mixture was stirred at low speed (800 revolutions per minute) and dispersed for 30 minutes to emulsify. And 12.5 mL (0.16 mol) of epichlorohydrin was added to the emulsified product, and after reacting for 20 minutes, it was filtered under pressure, and the filtered product was washed 5 times with hexane, and finally the product was vacuum dried to obtain an olefin polymerization catalyst carrier Z2.

[0106] Characterized by nuclear magnetic resonance and elemental analysis, the structural formula of the obtained catalyst carrier Z2 is as follows:

[0107]

[0108] The average particle diameter (D50) of...

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Abstract

The invention relates to the field of olefin catalysts, in particular to a catalyst component for olefin polymerization, an application of the catalyst component for olefin polymerization to preparation of a catalyst for olefin polymerization, the catalyst for olefin polymerization, an application of the catalyst to an olefin polymerization reaction and an olefin polymerization method. With the adoption of the technical scheme, the catalyst which is prepared from the catalyst component containing magnesium element, titanium element, manganese element and / or chromium element and specific internal electron donors selected from one or more of carboxylic ester, alcohol ester, ether, ketone, nitrile, amine and silane is higher in activity when applied to olefin polymerization or copolymerization, and content of ethylene structure units in polymers can also be increased when the catalyst is applied to copolymerization.

Description

Technical field [0001] The present invention relates to the field of olefin catalysts, in particular to a catalyst component for olefin polymerization, the application of the catalyst component for olefin polymerization in preparing a catalyst for olefin polymerization, and a catalyst for olefin polymerization , The application of the catalyst in the olefin polymerization reaction and an olefin polymerization method. Background technique [0002] As we all know, when the Ziegler-Natta catalyst supported by magnesium chloride alcoholate is used in the polymerization of olefins (especially propylene), its performance is significantly better than that of other supported catalysts. Therefore, most of the catalysts currently used for olefin polymerization are prepared by supporting titanium halide on magnesium chloride alkoxide. In order to obtain a spherical carrier, it can be prepared by spray drying, spray cooling, high-pressure extrusion, high-speed stirring, emulsifier method, a...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F10/00C08F110/06C08F210/06C08F4/629C08F4/626C08F4/631C08F4/634C08F4/02C08F4/609C08F4/606C08F4/611C08F4/614
CPCC08F10/00C08F110/06C08F210/06C08F210/16C08F2500/18C08F4/6294C08F4/6265C08F4/631C08F4/6343C08F4/022C08F4/6094C08F4/6065C08F4/611C08F4/6143
Inventor 凌永泰夏先知刘月祥李威莅任春红谭扬赵瑾高富堂彭人琪陈龙张天一张志会万真马长友段瑞林
Owner CHINA PETROLEUM & CHEM CORP