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Polyolefin and preparation method thereof

A polyolefin and olefin technology, applied in the field of polyolefin and its preparation, can solve the problems that restrict the development and application of high isotactic polyolefin alloys, reduce Vicat softening point, and reduce product performance, so as to improve polymerization activity and product specifications. Degree, improve catalytic activity, improve the effect of heat resistance

Active Publication Date: 2018-06-22
CHAMBROAD CHEM IND RES INST CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] Studies have shown that although polyolefin alloys have effectively improved the phase interface and two-phase dispersion problems between different polyolefin products in polyolefin alloys to a certain extent, thereby improving the performance of the products, due to the introduction of the second monomer, especially for For high-isotactic polyolefin alloy products, the differences in molecular chains of different polyolefins will lead to a significant decrease in one or some properties of the product, especially the significant decrease in heat resistance
For example, in the polymerization of 1-butene, the introduction of propylene as a polymerization monomer increases the modulus of polybutene-1 and improves the processing cycle, but the Vicat softening point of polybutene alloy products is significantly reduced due to the introduction of polypropylene , restricting the development and application of high isotactic polyolefin alloys

Method used

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  • Polyolefin and preparation method thereof

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Experimental program
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Effect test

Embodiment 1

[0035] Through the refining system, 1.6kg of liquid-phase propylene and 0.4kg of ethylene were respectively refined;

[0036] After the 10L polymerization kettle was replaced with nitrogen and vacuumized, triethylaluminum, external electron donor diphenyldimethoxysilane and MgCl were put into the reaction kettle in sequence. 2 Loaded TiCl 4 Catalyst (titanium loading is 2.6wt%, internal electron donor is ester) 0.20g, put into propylene 1.0kg, hydrogen 1.0L, wherein Al / Ti=60 (molar ratio), Si / Ti=15 (molar ratio) . Through the DCS control system, the polymerization was controlled at a constant temperature of 60°C for 30 minutes, followed by evacuation and cooling.

[0037] When the temperature of the reaction kettle is lowered to 20°C, put 1.0kg of ethylene-propylene mixed solution, triethylaluminum, and external electron donor diphenyldimethoxysilane into the reaction kettle, and put in 1.0L of hydrogen gas, among which, the ethylene-propylene mixed solution Among them, eth...

Embodiment 2

[0039] Through the refining system, 1.6kg of liquid-phase propylene and 0.4kg of ethylene were respectively refined;

[0040] After the 10L polymerization kettle was replaced with nitrogen and vacuumized, triethylaluminum, external electron donor diphenyldimethoxysilane and MgCl were put into the reaction kettle in sequence. 2 Loaded TiCl 4 Catalyst (2.6wt% titanium loading, esters as internal electron donor) 0.22g, propylene 1.0kg, hydrogen 2L, wherein Al / Ti=60 (molar ratio), Si / Ti=15 (molar ratio). Through the DCS control system, the polymerization was controlled at a constant temperature of 60°C for 30 minutes, followed by evacuation and cooling.

[0041] After the temperature of the reactor is lowered to 20°C, put 1.0kg of ethylene-propylene mixed solution, triethylaluminum, and the external electron donor into the reactor, which is compounded by diphenyldimethoxysilane and dicyclohexyldimethoxysilane , drop into 1L of hydrogen, wherein, in the ethylene-propylene mixture...

Embodiment 3

[0043] Through the refining system, 4.0kg of liquid-phase propylene and 1.5kg of ethylene were respectively refined;

[0044] After the 10L polymerization kettle was replaced with nitrogen and vacuumized, triethylaluminum, external electron donor diphenyldimethoxysilane and MgCl were sequentially put into the 10L reaction kettle 2 Loaded TiCl 4 Catalyst (titanium loading is 2.6wt%, internal electron donor is ester) 0.36g, input propylene 2.5kg, hydrogen 4.0L, wherein Al / Ti=60 (molar ratio), Si / Ti=20 (molar ratio) . Through the DCS control system, control the polymerization at a constant temperature of 70°C for 60 minutes, and then evacuate and lower the temperature.

[0045] When the temperature of the 10L reactor is lowered to 20°C, transfer the catalytically active polypropylene particles in the 10L reactor to the 20L reactor with the help of liquid phase propylene, and put in 3.0kg of ethylene-propylene mixture, triethylaluminum, and an external electron donor For the co...

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Abstract

The invention provides a preparation method of polyolefin. According to the preparation method, polyolefin is prepared through two-segment polymerization, and external electron donors are respectivelyadded in the two-segment polymerization process. By optimizing a catalyst feeding process in the polyolefin preparation process, particularly an external electron donor feeding process, an overall synthesis process of the polyolefin can be affected, catalysis activity of a catalyst and stereoregularity of an obtained polyolefin product can be improved, and furthermore macro-properties such as mechanical properties and thermal resistance of the obtained polyolefin product can be improved. Due to adoption of the external electron donor feeding process provided by the invention, and on the basisthat the polyolefin can be easily processed and molded and has the advantage of high modulus, the defect that polyolefin is poor in low-temperature brittleness is alleviated, and meanwhile the thermal resistance of the polyolefin is improved; in addition, the situation that the thermal resistance of the polyolefin is remarkably degraded because of introduction of a second monomer component in thepolyolefin is avoided.

Description

technical field [0001] The invention relates to the technical field of high molecular polymers, in particular to a polyolefin and a preparation method thereof. Background technique [0002] Polyolefin is the largest variety among the three major synthetic materials. However, polyolefin products obtained by homopolymerization of olefins have their own defects. For example, the most prominent shortcomings of polypropylene are cold resistance, low temperature brittleness, poor weather resistance, insufficient rigidity, and poor dyeability. In order to overcome the deficiencies in certain properties of polyolefin products, improve the comprehensive performance of polyolefin products, and broaden its application fields, the concept of polyolefin alloying is proposed. Polyolefin alloys refer to polyolefin heterogeneous mixtures containing various olefin homopolymer or copolymer components. The reactor polyolefin alloy refers to the polyolefin heterogeneous copolymer produced by d...

Claims

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Application Information

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IPC IPC(8): C08F210/16C08F210/02C08F210/06C08F210/08C08F4/645C08F4/646
CPCC08F4/6455C08F4/6465C08F210/08C08F210/16C08F210/02C08F210/06
Inventor 李海艳马韵升刘振学张云奎贾福祥尚明勇董兆强丁其维张新财韩晓倩高雨韩立霞
Owner CHAMBROAD CHEM IND RES INST CO LTD
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