Preparation method of low-entanglement ultrahigh molecular weight polyolefin

An ultra-high molecular weight, polyolefin technology, applied in the field of olefin polymerization, can solve problems such as increasing the chain overlap of primary segments, and achieve the effects of suppressing chain overlap, simple preparation process and simple preparation method

Active Publication Date: 2018-12-28
NINGBO UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although the catalyst activity is high, the active sites of the catalyst are randomly scattered on the carrier

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Example Embodiment

Example 1

Purge the reaction device with high-purity nitrogen to remove air and water in the reaction device. 900 μmol of iron acetylacetonate / pyridine diimide catalyst (post transition metal catalyst) was dissolved in 10 ml of toluene (90 μmol / ml), and 0.9 μmol of vinyl trimethoxysilane was added and stirred for 1 h. After the catalyst component solution is monitored by laser particle size, heterogeneous catalyst component particles with a radius of 350 nm can be formed. Adjust the slurry polymerization reactor to 30°C, add 400ml of toluene, add 1ml of the above catalyst component solution, stir for 1min, 450μmol of triethylboron (the molar ratio of the cocatalyst to the catalyst component is 5), 1-octane Olefin (25bar), polymerize for 15min. The polyoctene is measured by a rotor rheometer at 160°C to determine the modulus versus time curve, and the initial storage modulus and the maximum storage modulus (the modulus when the storage modulus does not change with the test ti

Example Embodiment

Example 2

Purge the reaction device with high-purity nitrogen to remove air and water in the reaction device. 900 μmol of iron acetylacetonate / pyridine diimide catalyst (post transition metal catalyst) was dissolved in 10 ml of toluene (90 μmol / ml), and 0.9 μmol of vinyl trimethoxysilane was added and stirred for 1 h. After the catalyst component solution is monitored by laser particle size, heterogeneous catalyst component particles with a radius of 350 nm can be formed. Adjust the slurry polymerization reactor to 30°C, add 400ml of toluene, add 1ml of the above catalyst component solution, stir for 1min, 450μmol of triethylboron (the molar ratio of the cocatalyst to the catalyst component is 5), 1-octane Olefin (25bar), polymerize for 15min. The polyoctene is measured by a rotor rheometer at 160°C to determine the modulus versus time curve, and the initial storage modulus and the maximum storage modulus (the modulus when the storage modulus does not change with the test ti

Example Embodiment

Example 3

Purge the reaction device with high-purity nitrogen to remove air and water in the reaction device. 900 μmol of iron acetylacetonate / pyridine diimide catalyst (post transition metal catalyst) was dissolved in 10 ml of toluene (90 μmol / ml), and 0.9 μmol of vinyl trimethoxysilane was added and stirred for 1 h. After the catalyst component solution is monitored by laser particle size, heterogeneous catalyst component particles with a radius of 350 nm can be formed. Adjust the slurry polymerization reactor to 30°C, add 400ml of toluene, add 1ml of the above catalyst component solution, stir for 1min, 450μmol of triethylboron (the molar ratio of the cocatalyst to the catalyst component is 5), 1-octane Olefin (25bar), polymerize for 15min. The polyoctene is measured by a rotor rheometer at 160°C to determine the modulus versus time curve, and the initial storage modulus and the maximum storage modulus (the modulus when the storage modulus does not change with the test ti

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Abstract

The invention discloses a preparation method of low-entanglement ultrahigh molecular weight polyolefin. The preparation method of the low-entanglement ultrahigh molecular weight polyolefin comprises the following steps: (1) an active component and a nucleating agent are contacted in a solvent A in a molar ratio of 10 to 500 to obtain a catalyst component for later use, wherein the catalyst component is core-shell structured particles taking the active component as a shell and the nucleating agent as a core and having the radius of 100 to 2000nm; (2) an olefin monomer, a cocatalyst, a polymerization solvent and the catalyst component in the step (1) are added to a reactor to prepare ultrahigh molecular weight polyethylene, wherein the molar ratio of the cocatalyst to metal in the catalyst component is 0.1 to 10; the reaction temperature is minus 40 to 160 DEG C, the reaction time is 1 to 480min and the reaction pressure is 1 to 60bar; (3) the weight average molecular weight of the ultrahigh molecular weight polyethylene prepared in the step (2) is 1,000,000 to 10,000,000 g/mol, the ratio of the initial storage modulus to the maximum storage modulus is that GN<t>, and t=100 is equalto 0.1 to 0.75; the low-entanglement ultrahigh molecular weight polyolefin is prepared by activating an active center of the catalyst surface at a very low amount of the cocatalyst.

Description

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Claims

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Application Information

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Owner NINGBO UNIV
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