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Catalyst component for olefin polymerization, preparation method, catalyst and application thereof

A technology of olefin polymerization and catalyst, which is applied in the field of olefin polymerization catalysts, can solve problems such as crushing, increase in fine powder content, and unsatisfactory problems, and achieve the effects of low fine powder content, good hydrogen adjustment 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, preparation method, catalyst and application thereof
  • Catalyst component for olefin polymerization, preparation method, catalyst and application thereof
  • Catalyst component for olefin polymerization, preparation method, catalyst and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0089] (1) Preparation of catalyst components

[0090] To a four-port flask equipped with a temperature controller, a stirrer, a reflow condenser, a 450 ml of nitrogen, and a 120 ml of tetrahydrofuran (THF), 4.2 g of magnesium chloride and 1.0 ml of TiCl were added under stirring. 4 , The temperature was warmed to 68 ° C with stirring, and the constant temperature reflux was 4 hours at this temperature to obtain a mother liquor;

[0091] To a temperature controller, a stirrer, a reflow condenser, a four-mouth flask blown and protected by nitrogen, and the Cabot Corporation TS-610, a particle size of less than 1 μm) and 1.0 g eight Methyl polyfangular polycarcane, silica gel and octamethylene polyfriendin polymethylenesiloxane weight ratio 5.5, adding the mother liquor, continued constant temperature and reflux for 2 hours at 68 ° C, complete silicone Dispersed in the mother liquor to give a slurry suspension;

[0092] In closed circuit circulating airflow spray dryer (such as MIN...

Embodiment 2

[0096] As compared with Example 1, only in the preparation of the catalyst component of step (1) "Add 5.5 g of silica gel (CabotcorPoration TS-610, particle size less than 1 μm) and 1.0 g of octamethylene polymerizing polylinediloxane, The weight ratio of silica gel and multi-neutral polysiloxane is "changed to" to add 6.4 g of silica gel (Cabot Corporation TS-610, particle size less than 1 μm) and 0.1 g of octamethylene polyfriendin polymethylenesiloxane, silicone The weight ratio 64 of the multipolar neutralized semi-silicone oxide is the same as those in Example 1. Among them, the Poss content in the calculation catalyst is 0.55% by weight, and the content analysis of other components is shown in Table 1, the margin is the carrier.

Embodiment 3

[0098] As compared with Example 1, only in the preparation of the catalyst component of step (1) "Add 5.5 g of silica gel (CabotcorPoration TS-610, particle size less than 1 μm) and 1.0 g of octamethylene polymerizing polylinediloxane, The weight ratio of silica gel and multi-neutral polysiloxane is 5.5 "Change to" to add 6.0 g of silica gel (Cabot Corporation TS-610, particle size of less than 1 μm) and 0.5 g of octamide polymerizing polycarbilisiloxane, silicone The weight ratio 12 of the multipolar hemoxyside is the same as those in Example 1. Wherein the catalyst has been calculated POSS content of 2.73wt%, the content of the other components of the analysis are shown in Table 1, the balance being a carrier.

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Abstract

The invention discloses a catalyst component for olefin polymerization, a preparation method of the catalyst component, a catalyst and an application of the catalyst component, and the catalyst component comprises a titanium element, a magnesium element, an electron donor, polyhedral oligomeric silsesquioxane and an inorganic oxide carrier, the catalyst component is obtained by mixing raw materials including a titanium-containing compound, magnesium halide, an electron donor, polyhedral oligomeric silsesquioxane and an inorganic oxide carrier and then performing spray drying. The catalyst comprises the catalyst component and an organic aluminum compound, and has the characteristics of high activity, good hydrogen regulation copolymerization performance, high bulk density of obtained polymer powder and low fine powder content when being used for olefin polymerization, especially polymerization of ethylene and alpha-olefin.

Description

Technical field [0001] The present invention relates to an olefin polymerization catalyst, and in particular, to catalyst components, preparation methods and catalysts for olefin polymerization. Background technique [0002] It is well known that olefin polymerization high-efficiency Ziegler-Natta catalyst consists of two parts of the main catalyst and cocatalyst. The main catalyst is composed of a transition metal compound located in the fourth to eighth host group in the periodic table, and the cocatalyst is a metal organic compound located in the first to third main chaces in the periodic table. Typically, the main catalyst can also be divided into two parts: an inert carrier and its load active component. The preparation of the main catalyst generally uses titanium halides to react with a halide reaction with a lattice defective magnesium or a reactant load is prepared on an inert carrier. The compound in which magnesium-based compounds is good, while the halide having a latt...

Claims

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Application Information

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IPC IPC(8): C08F10/00C08F10/02C08F4/02C08F4/649C08F110/02
CPCC08F10/00C08F10/02C08F110/02C08F4/025C08F4/6498C08F2500/12C08F2500/18C08F2500/24Y02P20/52
Inventor 崔楠楠郭子芳李秉毅王如恩傅捷闫力欣寇鹏徐世媛
Owner CHINA PETROLEUM & CHEM CORP