Highly active supporting method of non-metallocene catalyst

A non-metallocene and catalyst technology, applied in the field of supported non-metallocene catalysts, can solve the problems of low catalytic activity, uneconomical application of supported catalysts, and reduced catalytic olefin polymerization activity.

Active Publication Date: 2006-06-21
SINOPEC YANGZI PETROCHEM
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0008] Catalysts supported on anhydrous magnesium chloride show high catalytic activity in olefin polymerization, but such catalysts are very brittle and break easily in the polymerization reactor, resulting in poor polymer morphology
Silica-supported catalysts have good fluidity and can be used in gas-phase fluidized bed polymerization, but silica-supported metallocene and non-metallocene catalysts show lower catalytic activity
However, after the non-metallocene catalyst is supported by an inert carrier, the catalyti

Method used

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Embodiment 1

[0070] Embodiment 1, the highly active loading method of non-metallocene catalyst, mainly comprises the following steps:

[0071] The porous solid of the carrier adopts silica gel Grace 955, and the silica gel is heated at 500-800°C and N 2 Or continue drying or roasting under Ar atmosphere for 4-8h. Heat-activated dehydroxylated silica gel needs to be stored under an inert atmosphere.

[0072] The chemical activator adopts titanium tetrachloride; the activated carrier is reacted with titanium tetrachloride, and the modified carrier is obtained after filtering, washing, drying and pumping. The mass ratio of titanium tetrachloride and silica gel is 1: 40;

[0073] Magnesium chloride is dissolved in a tetrahydrofuran-ethanol mixed system to form a solution, and then the modified carrier is added into the solution, and fully reacted under the stirring condition of 0-60° C. to form a transparent system. The time is 1 to 48 hours, preferably 4 to 24 hours. The composite carrier...

Embodiment 1-1

[0081] Embodiment 1-1 is basically the same as Embodiment 1, but has the following changes:

[0082] Dissolve magnesium fluoride in tetrahydrofuran-methanol mixed system to form a solution.

Embodiment 1-2

[0083] Embodiment 1-2 is basically the same as Embodiment 1, but has the following changes:

[0084] Dissolve magnesium iodide in tetrahydrofuran-propanol mixed system to form a solution.

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Abstract

A method of non- metallocene catalyst loading with high active: the carrier and chemical activating agent reacting with each other to get the modification carrier; dissolving the magnesium compounds into the tetrahydrofuran-alcohol mixing system to form solution, adding the modification carrier into the solution for reaction, filtering, washing, drying and sucting to get the composite carrier; dissolving the non- metallocene catalyst for lkene polymerization into the dissolvent, then reacting with the composite carrier and through process of washing, filtering and drying to get the load non- metallocene catalyst. It can also be: proceeding heating activating treatment before the reaction of carrier with the chemical activating agent; the composite carrier reacting with chemical additive before reacting with catalyst to get the modification composite carrier, the modification composite carrier reacting with catalyst to get the load non- metallocene catalyst. The load catalyst produced in this invention is high active; the load catalyst of high property can be produced with less methylaluoxane; the polyolefine produced with the catalyst prepared in this invention possesses sound granual shape.

Description

technical field [0001] The invention belongs to the technical field of catalyst loading, and relates to a loading method of a non-metallocene catalyst, which is a non-metallocene olefin polymerization catalyst loaded on a composite carrier, and a highly active loaded non-metallocene catalyst is obtained by loading . The composite carrier-supported non-metallocene catalyst can be used for catalyzing olefin polymerization and copolymerization, especially for catalyzing the homopolymerization of ethylene or the copolymerization of ethylene and other α-olefins. Background technique [0002] Homogeneous transition metal catalysts known to be highly active in olefin polymerization, such as unsupported Ziegler-Natta catalysts, metallocene olefin polymerization catalysts, constrained geometry olefin polymerization catalysts or non-metallocene olefin polymerization catalyst. The coordination atoms of non-metallocene olefin polymerization catalysts are oxygen, nitrogen, sulfur and c...

Claims

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Application Information

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IPC IPC(8): C08F10/00C08F4/02C08F4/50
Inventor 戴厚良尤侯平李传峰姚小利王亚明周立进马忠林李晓强柏基业
Owner SINOPEC YANGZI PETROCHEM
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