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A kind of production method of impact-resistant polypropylene

A production method and polypropylene technology, which can be applied in the production of bulk chemicals and other directions, can solve problems such as increased production costs and reduced activity.

Active Publication Date: 2017-09-26
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the biggest disadvantage of this method is that the activity of the commonly used Zigler-Natta catalyst decays rapidly at a temperature higher than 80°C, which greatly increases the production cost of the product.

Method used

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  • A kind of production method of impact-resistant polypropylene
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  • A kind of production method of impact-resistant polypropylene

Examples

Experimental program
Comparison scheme
Effect test

preparation example 1

[0048] The component (a) in the catalyst used in the preparation method of the present invention is the titanium-containing solid catalyst component.

[0049] A 16L pressure-resistant reactor with a stirrer was fully replaced with nitrogen, and then 10L of ethanol, 300mL of 2-ethylhexanol, 11.2g of iodine, 8g of magnesium chloride and 640g of magnesium powder were added to the reactor. While stirring, the system was refluxed until no more hydrogen was emitted. Stop the reaction, wash with 3L ethanol, filter and dry. The resulting dialkoxymagnesium support. The obtained dialkoxymagnesium carrier has a D50 of 30.2 μm, a span value of 0.81, and an m value of 0.015. Take 650 g of the above-mentioned dialkoxymagnesium carrier and 3250 mL of toluene to prepare a suspension. In a 16L pressure-resistant reactor that has been repeatedly replaced by high-purity nitrogen, add 2600 mL of toluene and 3900 mL of titanium tetrachloride, raise the temperature to 80 ° C, then add the prepar...

preparation example 2

[0051] The component (a) in the catalyst used in the preparation method of the present invention is the titanium-containing solid catalyst component.

[0052] Take 650 g of the dialkoxymagnesium carrier in Preparation Example 1, 3250 mL of toluene and 65 mL of 2-isopropyl-2-isopentyl-1,3-dimethoxypropane to prepare a suspension. In a 16L pressure-resistant reaction kettle that has been repeatedly replaced by high-purity nitrogen, add 2600mL of toluene and 3900mL of titanium tetrachloride, raise the temperature to 80°C, then add the prepared suspension into the kettle, keep the temperature for 1 hour, and add 2-isopropyl Base-2-isoamyl-1,3-dimethoxypropane (1# ether) 65mL, slowly heated to 110°C, kept at constant temperature for 2 hours, and press-filtered to obtain a solid. The resulting solid was added to a mixed solution of 5070 mL of toluene and 3380 mL of titanium tetrachloride and stirred at 110° C. for 1 hour, and treated like this three times. Pressure filtration, the ...

Embodiment 1

[0053] The preparation of embodiment 1 impact polypropylene

[0054] The preparation of impact polypropylene in the present invention is all in figure 1completed on the device shown. The device is a set of pilot scale propylene polymerization gas phase reaction device with an output of 40kg / hr, of which 9 and 17 are horizontal stirred bed reactors. The horizontal stirred bed reactor is well known in the industry. It is a horizontally placed reactor with agitation. The polymerization catalyst and part of the reaction raw materials are added from one end of the reactor. The reactor is discharged from the end, and the function of stirring in the reactor is to cause the material to mix in the radial direction, without the effect of axial pushing or back mixing. Catalyst component (a) is as feed stream 1, and catalyst component (b) and component (c) are as feed stream 2, are respectively carried into the first reactor 9 by fresh propylene, carry out in the first reactor 9 Homop...

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Abstract

The present invention relates to a production method of impact polypropylene, comprising two stages of polymerization: A. Homopolymerization of propylene: at a polymerization temperature of 50°C to 120°C, propylene is carried out in a gas phase or a liquid phase medium in the presence of a catalyst Homopolymerization reaction to obtain a propylene homopolymer; B. Propylene-ethylene copolymerization: In the presence of the propylene homopolymer obtained in step A at a polymerization temperature of 50°C to 120°C, the copolymerization reaction of propylene and ethylene is carried out in a gas phase medium, An impact polypropylene with a high ethylene content is obtained. Through the synergistic effect of the method and the catalyst, the polymerization temperature range in the ethylene-propylene copolymerization stage reactor is raised from the conventional 60°C to 80°C to 60°C to 120°C, which effectively improves the circulation gas heat exchanger. Thermal capacity, the catalyst can still maintain a high polymerization activity at a higher reaction temperature.

Description

technical field [0001] The invention relates to a production method of impact-resistant polypropylene with high ethylene content and belongs to the field of polymer production. Background technique [0002] Impact polypropylene is usually a heterogeneous mixture of polypropylene produced by multiple reactors in series. Generally, propylene is homopolymerized in the first reactor to obtain isotactic polypropylene, which is then sent to the next reactor for propylene Copolymerization with ethylene produces a polymer mainly composed of ethylene-propylene random copolymers in the pores of propylene homopolymer particles. Therefore, impact polypropylene, especially impact polypropylene products with high ethylene content (ethylene content higher than 12%, wt, the same below), has a good balance of rigidity and toughness, and has been widely used in automobiles, household appliances and Daily necessities and other fields. [0003] At present, most impact polypropylene grades use...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F210/06C08F4/649
CPCY02P20/52
Inventor 陈江波于鲁强杨芝超仝钦宇杜亚锋刘旸张雅茹
Owner CHINA PETROLEUM & CHEM CORP