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Catalyst composition for long-chain alpha-olefin polymerization and method for catalyzing long-chain alpha-olefin polymerization by catalyst composition

A technology of olefin polymerization and catalyst, which is applied in the field of catalysts for olefin polymerization, and can solve the problems of poor thermal stability and high molecular weight of catalyzed long-chain α-olefins

Active Publication Date: 2018-02-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0006] The purpose of the present invention is to provide a catalyst combination for the polymerization of long-chain α-olefins in view of the technical deficiencies such as the poor thermal stability of the existing α-diimine nickel metal catalyst and the high molecular weight of catalyzed long-chain α-olefins The compound and the method for catalyzing the polymerization of long-chain α-olefins make the catalyst composition have high catalytic activity and good thermal stability when catalyzing the chain transfer polymerization of α-olefins, and are used for synthesizing polyα-olefins with controllable molecular weight

Method used

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  • Catalyst composition for long-chain alpha-olefin polymerization and method for catalyzing long-chain alpha-olefin polymerization by catalyst composition
  • Catalyst composition for long-chain alpha-olefin polymerization and method for catalyzing long-chain alpha-olefin polymerization by catalyst composition
  • Catalyst composition for long-chain alpha-olefin polymerization and method for catalyzing long-chain alpha-olefin polymerization by catalyst composition

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0054] The 100ml three-necked reaction flask was evacuated, replaced three times with nitrogen, and 8.3mg (10μmol) of complex 2, 15ml of 1-decene, 0.8ml of methylaluminoxane (MAO) (1.53mol / l toluene solution) were added successively. , 0.5ml of diethylzinc (1.0mol / l toluene solution), the polymerization reaction was stopped after 2 hours at 90°C, and the reaction system was black and viscous. The reaction was terminated with a dilute hydrochloric acid-ethanol solution, the obtained polymer was dissolved in tetrahydrofuran, and precipitated with methanol. This was repeated three times. Finally, the sample was placed in a vacuum drying oven for drying for 24 hours to obtain 3.10 g of a white solid polymer with a certain elasticity. . The catalytic efficiency of the catalytic system is 310 kg mol -1 Ni, the weight-average molecular weight of the polymer measured at the end of the reaction was Mw=256,200, and the molecular weight distribution was Mw / Mn=2.41.

Embodiment 2

[0064] The 100ml three-necked reaction flask was evacuated, replaced three times with nitrogen, and 8.3mg (10μmol) of complex 2, 15ml of 1-decene, 0.8ml of methylaluminoxane (MAO) (1.53mol / l toluene solution) were added successively. , 1.0ml of diethylzinc (1.0mol / l toluene solution), the polymerization reaction was stopped after 2 hours at 90°C, and the reaction system was black and viscous. The reaction was terminated with a dilute hydrochloric acid-ethanol solution, the obtained polymer was dissolved in tetrahydrofuran, and precipitated with methanol. This was repeated three times. Finally, the sample was placed in a vacuum drying oven for drying for 24 hours to obtain 3.64 g of a white solid polymer with a certain elasticity. . The catalytic efficiency of the catalytic system is 364 kg mol -1 Ni, the weight-average molecular weight of the polymer measured at the end of the reaction was Mw=142,400, and the molecular weight distribution was Mw / Mn=2.07.

Embodiment 3

[0066] The 100ml three-necked reaction flask was evacuated, replaced three times with nitrogen, and 8.3mg (10μmol) of complex 2, 15ml of 1-decene, 0.8ml of methylaluminoxane (MAO) (1.53mol / l toluene solution) were added successively. , 2.0ml of diethylzinc (1.0mol / l toluene solution), the polymerization reaction was stopped after 2 hours at 90°C, and the reaction system was black and viscous. The reaction was terminated with a dilute hydrochloric acid-ethanol solution, the obtained polymer was dissolved in tetrahydrofuran, and precipitated with methanol. This was repeated three times. Finally, the sample was placed in a vacuum drying oven to dry for 24 hours to obtain 1.92 g of a polymer with certain elasticity. The catalytic efficiency of the catalytic system is 192 kgmol -1 Ni, the weight-average molecular weight of the polymer measured at the end of the reaction was Mw=86,400, and the molecular weight distribution was Mw / Mn=2.27.

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Abstract

The invention provides catalyst composition for long-chain alpha-olefin polymerization and a method for catalyzing long-chain alpha-olefin polymerization by the catalyst composition. The catalyst composition contains a main catalyst, a catalyst promoter and a chain transfer agent, wherein the main catalyst is a complex with the chemical structure shown in the description, R<1>-R<10> are the same or different and are independently selected from hydrogen, saturated or unsaturated alkyl, alkoxy or halogen, and X is selected from halogen; the catalyst promoter is selected from at least one of alkylaluminoxane, aromatic boron and borate; the chain transfer agent is selected from trialkylaluminium and / or dialkylzinc. The method for catalyzing long-chain alpha-olefin polymerization by the catalyst composition comprises the step as follows: long-chain alpha-olefin, the main catalyst, the catalyst promoter and the chain transfer agent are contacted for the polymerization reaction in the presence of inert gas. When catalyzing chain-transfer polymerization of alpha-olefin, the catalyst composition has higher catalytic activity and good heat stability and is used for synthesizing poly alpha-olefin with controllable molecular weight.

Description

technical field [0001] The present invention relates to the technical field of catalysts for olefin polymerization, and more particularly, to a catalyst composition for chain transfer polymerization of long-chain alpha-olefins and a method for catalyzing the polymerization of long-chain alpha-olefins. Background technique [0002] Poly-alpha-olefin synthetic oil (PAO) is a high-purity oil produced by oligomerization and hydrogenation of alpha-olefin under the action of a catalyst. Compared with mineral oil, PAO has the characteristics of high viscosity index, low pour point, high flash point and excellent high and low temperature performance, and it is still irreplaceable in many oil products. A significant subject in the preparation of α-olefin synthetic oil is to explore a method for controlling the viscosity index of poly-α-olefin, that is, controlling the molecular weight and distribution of poly-α-olefin. [0003] Single-active-site polyolefin catalysts can well contro...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F10/14C08F110/14C08F4/70C08F2/38
CPCC08F10/14C08F110/14C08F4/7006C08F2/38C08F2500/03C08F2500/02
Inventor 高榕赖菁菁李岩刘东兵郭子芳周俊领廖浩瀚傅捷
Owner CHINA PETROLEUM & CHEM CORP