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Catalyst component for olefin polymerization or copolymerization as well as preparation method and application of catalyst component

An olefin polymerization and catalyst technology, applied in the field of olefin polymerization catalysts, can solve the problems of fragmentation, rising fine powder content, unsatisfactory and other problems, and achieve the effects of low fine powder content, good hydrogen regulation performance and high bulk density

Pending Publication Date: 2021-10-29
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] CN1802391A discloses a catalyst for ethylene polymerization prepared by a spray drying process. The catalyst has good activity, but in the gas phase polymerization, serious fragmentation will still occur and cause the fine powder content to rise
[0008] Some of the above-mentioned various catalysts can only improve the performance of olefin polymerization catalysts in a certain aspect, although some can improve several performances, they are still not ideal.

Method used

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  • Catalyst component for olefin polymerization or copolymerization as well as preparation method and application of catalyst component
  • Catalyst component for olefin polymerization or copolymerization as well as preparation method and application of catalyst component

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0088] (1) Preparation of catalyst components

[0089] To a 250mL four-necked flask equipped with a temperature controller, a stirrer, and a reflux condenser, which was purged and protected with nitrogen, 120mL of tetrahydrofuran (THF), 4.2g of magnesium chloride and 1.0mL of TiCl were successively added under stirring. 4 , heated up to 68° C. under stirring, and refluxed at this temperature for 4 hours to obtain the mother liquor;

[0090] Into a 250 mL four-necked flask equipped with a temperature controller, a stirrer, and a reflux condenser, which was purged and protected with nitrogen, 5.5 g of silica gel (Cabot Corporation TS-610, particle size less than 1 μm) and 1.0 g of organic Silicone polymer [with (CH 3 ) 2 SiCl 2 and (CH 3 ) SiCl 3 To mix the monomers, control the value of r / s to 1.3, and co-hydrolyze the mixed monomers to obtain a network-structured organosilicon polymer], the weight ratio of silica gel to organosilicon polymer is 5.5, add the above mother l...

Embodiment 2

[0095] Compared with Example 1, only in the preparation of step (1) catalyst component "add 5.5g silica gel (Cabot Corporation TS-610, particle diameter is less than 1 μm) and 1.0g organosilicon polymer (with (CH 3 ) 2 SiCl 2 and (CH 3 ) SiCl 3 To mix the monomers, control the value of r / s to 1.3, and co-hydrolyze the mixed monomers to obtain a network-structured silicone polymer), and the weight ratio of silica gel to silicone polymer is 5.5" to "add 6.4 grams of silica gel (Cabot Corporation TS-610, particle size less than 1μm) and 0.1g silicone polymer (in the form of (CH 3 ) 2 SiCl 2 and (CH 3 ) SiCl 3 For the mixed monomer, the value of r / s is controlled to be 1.3, and the mixed monomer is co-hydrolyzed to obtain the organosilicon polymer of the network structure), the weight ratio of silica gel to the organosilicon polymer is 64", and the others are the same as in Example 1. Wherein , the content of organosilicon polymer in the catalyst is calculated to be 0.585w...

Embodiment 3

[0097] Compared with Example 1, only in the preparation of step (1) catalyst component "add 5.5g silica gel (Cabot Corporation TS-610, particle diameter is less than 1 μm) and 1.0g organosilicon polymer (with (CH 3 ) 2 SiCl 2 and (CH 3 ) SiCl 3 To mix the monomers, control the value of r / s to 1.3, and co-hydrolyze the mixed monomers to obtain a network-structured organosilicon polymer), and the weight ratio of silica gel to organosilicon polymer is 5.5" to "add 6.0 grams of silica gel (Cabot Corporation TS-610, particle size less than 1μm) and 0.5g silicone polymer (in the form of (CH 3 ) 2 SiCl 2 and (CH 3 ) SiCl 3 For the mixed monomer, the value of r / s is controlled to be 1.3, and the mixed monomer is co-hydrolyzed to obtain the organosilicon polymer with a network structure), the weight ratio of silica gel to the organosilicon polymer is 12", and the others are the same as in Example 1. Wherein , the content of organosilicon polymer in the catalyst was calculated t...

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Abstract

The invention discloses a catalyst component for olefin polymerization or copolymerization and a preparation method and an application thereof, and the catalyst component comprises a titanium element, a magnesium element, an electron donor, an organosilicon polymer and an inorganic oxide carrier. The organosilicon polymer is obtained by hydrolyzing one or more monomers with a general formula of RxSiCl (4-x), R is selected from alkyl, aryl, vinyl or hydrogen, x is an integer of 0-3, and when x is greater than 1, the substituent groups R are the same or different. The catalyst component is obtained by mixing raw materials including a titanium-containing compound, magnesium halide, an electron donor, an organosilicon polymer and an inorganic oxide carrier and then performing spray drying. The catalyst prepared from the catalyst component can be used for olefin polymerization, especially for ethylene and alpha-olefin polymerization, and has the characteristics of high activity, good hydrogen regulation copolymerization performance, high bulk density of obtained polymer powder, and low fine powder content of the polymer powder.

Description

technical field [0001] The invention relates to an olefin polymerization catalyst, in particular to a catalyst component for olefin polymerization or copolymerization, a preparation method, a catalyst and applications thereof. Background technique [0002] It is well known that the high-efficiency Ziegler-Natta catalyst for olefin polymerization consists of two parts: the main catalyst and the co-catalyst. The main catalyst is composed of a transition metal compound located in the fourth to eighth main groups of the periodic table, and the cocatalyst is a metal organic compound located in the first to third main groups of the periodic table. Usually, the main catalyst can be divided into two parts: an inert carrier and its supported active component. The main catalyst is generally prepared by reacting titanium halides with magnesium halides with lattice defects or by loading the reactants on an inert carrier. Wherein the magnesium compound is preferably a magnesium halide ...

Claims

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Application Information

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IPC IPC(8): C08F10/00C08F110/02C08F4/649C08F4/646C08F4/02
CPCC08F10/00C08F110/02C08F4/6494C08F4/6465C08F4/025C08F2500/18C08F2500/12C08F2410/06Y02P20/52C08F4/6565C08F2500/24C08F10/02C08F210/16C08F210/02C08F4/65916C08F4/654C08F4/02C08F4/6425C08F4/6498
Inventor 崔楠楠郭子芳李秉毅王如恩李岩傅捷闫力欣安京燕寇鹏徐世媛张彤瑄
Owner CHINA PETROLEUM & CHEM CORP