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Catalyst composition for ethylene gas-phase polymerization or co-polymerization, preparation and applications thereof

A gas-phase polymerization and catalyst technology, applied in the field of bimetallic silica gel carrier catalyst composition and preparation thereof, can solve the problems of narrow molecular weight distribution of polyethylene resin, difficulty in achieving complete and uniform blending of resin, affecting the final performance of resin, etc.

Active Publication Date: 2014-10-01
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

That is to mix resins with different molecular weights in a molten state. This method is not only costly, but also difficult to achieve complete and uniform blending of the resins, which affects the final properties of the resins;
[0004] (2) By performing staged polymerization in multi-stage reactors, a relatively uniform resin can be obtained, and the operation and adjustment flexibility is relatively large, but there are problems affecting efficiency and high cost;
[0008] Chinese patent CN101225129A discloses that a composite catalyst composed of two late transition metals iron and nickel is used to prepare bimodal polyethylene, but the required cocatalyst is generally methyl aluminoxane, resulting in higher production costs of bimodal polyethylene
[0010] As can be seen from the catalysts disclosed in the above-mentioned patents, although the multi-active center catalysts formed by two or more Ziegler-Natta type catalyst components can be used to prepare broad distribution or bimodal distribution polyethylene resins, there is still activity. The low problem is generally below 100,000 g / g metal; and for the Ti / V catalyst system disclosed in Chinese patent CN88101779, the molecular weight distribution of the obtained polyethylene resin is also relatively narrow, and its melt flow ratio (MFR) is 40 ~70

Method used

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  • Catalyst composition for ethylene gas-phase polymerization or co-polymerization, preparation and applications thereof
  • Catalyst composition for ethylene gas-phase polymerization or co-polymerization, preparation and applications thereof
  • Catalyst composition for ethylene gas-phase polymerization or co-polymerization, preparation and applications thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] Preparation of bimetallic catalyst composition:

[0047] (1) Weigh 20g of spherical silica gel (produced by Grace Company in the United States, with an average particle size of 45μm and a specific surface area of ​​350m 2 / g), put silicon dioxide in a gas-phase fluidized bed activator, blow and fluidize it with anhydrous and oxygen-free nitrogen, gradually raise the temperature to 600°C, and dehydrate at constant temperature for 6 hours to obtain dehydrated silicon dioxide.

[0048] (2) Add 100mL of isopentane to a reaction flask with a stirrer under nitrogen protection, add 10g of silica gel after thermal activation treatment in step (1) and 5.6mL of AlEt with a concentration of 1mmol / mL 3 Add the hexane solution, react at 20-30°C for 1 hour, heat to evaporate the alkane solvent, and obtain fluid activated silica.

[0049] (3) In another reaction flask with a stirrer, add 0.64mL TiCl 4 , 2,6-bis[1-(2,6-dimethylbenimine)ethyl]pyridine ferric dichloride 0.0968g, 1.74g ...

Embodiment 2

[0055] Preparation of bimetallic catalyst composition:

[0056] (1) Weigh about 20g of spherical silica gel (produced by Grace Company in the United States, with an average particle size of 45μm and a specific surface area of ​​350m 2 / g), put silicon dioxide in a gas-phase fluidized bed activator, blow and fluidize it with anhydrous and oxygen-free nitrogen, gradually raise the temperature to 600°C, and dehydrate at constant temperature for 4 hours to obtain dehydrated silicon dioxide.

[0057] (2) Add 100mL of isopentane to a reaction flask with a stirrer under nitrogen protection, add 10g of silica gel after thermal activation treatment in step (1) and 5.6mL of AlEt with a concentration of 1mmol / mL 3 Add the hexane solution, react at 20-30°C for 1 hour, heat to evaporate the alkane solvent, and obtain fluid activated silica.

[0058] (3) In another reaction flask with a stirrer, add 0.64mL TiCl 4 , 2,6-bis[1-(2,6-dimethylbenimine)ethyl]pyridine ferric dichloride 0.1937g, ...

Embodiment 3

[0064] Preparation of catalyst composition

[0065] (1) Weigh about 20g of spherical silica gel (produced by Grace Company in the United States, with an average particle size of 55μm and a specific surface area of ​​278m 2 / g), put silicon dioxide in a gas-phase fluidized bed activator, blow and fluidize it with anhydrous and oxygen-free nitrogen, gradually raise the temperature to 600°C, and dehydrate at constant temperature for 10 hours to obtain dehydrated silicon dioxide.

[0066] (2) Add 100mL of isopentane to a reaction flask with a stirrer under nitrogen protection, add 10g of silica gel after thermal activation treatment in step (1) and 5.6mL of AlEt with a concentration of 1mmol / mL 3 Add the hexane solution, react at 20-30°C for 1 hour, heat to evaporate the alkane solvent, and obtain fluid activated silica.

[0067] (3) In another reaction flask with a stirrer, add 1.74g MgCl 2 , 2,6-bis[1-(2,6-dimethylbenimine)ethyl]pyridine ferric dichloride 0.3874g, 0.64mL TiCl 4...

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Abstract

The invention relates to a catalyst composition for ethylene gas-phase polymerization or co-polymerization, preparation and applications thereof. The preparation method comprises the following steps: dissolving a titanium compound, an iron compound, and a magnesium compound in tetrahydrofuran so as to obtain a mother liquid; adding a modified silica carrier, which has been subjected to a thermal treatment and a chemical treatment, into the mother liquid, carrying out refluxing for 1 hour under stirring, blow-drying the mother liquid with high-purity nitrogen gas to remove the excess tetrahydrofuran, controlling the residual tetrahydrofuran content to be in a range of 10 to 15 wt% of the total weight of the product, floating the obtain solid in a low-carbon alkane solvent, carrying out a reduction treatment for 30 minutes on the solid at a room temperature by using one or more alkyl aluminum compounds, and then blow-drying the product with high-purity nitrogen gas so as to obtain the catalyst composition. The catalyst has a high catalytic activity when the catalyst is used to catalyze ethylene polymerization especially the gas-phase fluidized bed polymerization; and can prepare polyethylene products with a wide molecular weight distribution or double-peak distribution. The prepared polyethylene product has a high bulk density and little fine powder.

Description

technical field [0001] The invention relates to a catalyst suitable for producing bimodal or broad-modal distribution polyethylene in a single reactor and a preparation method thereof, in particular to a bimetallic silica gel carrier catalyst composition suitable for ethylene polymerization or copolymerization and its preparation method. Background technique [0002] Polyethylene resin is one of the four major synthetic resins. High-performance polyethylene resin must have high toughness, high strength and high environmental stress cracking resistance. Increasing the molecular weight of polyethylene can lead to a corresponding improvement in these properties. However, as the molecular weight of the polymer increases, the processability of the resin generally decreases. By preparing polymers with a broad or bimodal molecular weight distribution, not only can the characteristic properties of high molecular weight resins be maintained, but the processability of the resins can...

Claims

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Application Information

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IPC IPC(8): C08F10/02C08F2/34C08F4/02C08F4/70
CPCY02P20/52
Inventor 何书艳姜涛邹恩广杨家靖赵成才付义王斯晗苏杭张瑀健王兆武姜进宪高宇新李明权马丽王立娟赵增辉任鹤任合刚王世华杨立伟李洪兴李文邴淑秋汪涵于秀娟
Owner PETROCHINA CO LTD
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