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Polymerization reactor and method for producing polypropylene by employing the same

A polymerization reactor and polypropylene technology, which is applied in the field of propylene-ethylene-butene terpolymer random copolymer, can solve the problems of uneven particle size of polypropylene polymer, uneven residence time of catalyst, and backward shift of catalyst activity, etc. , to achieve the effects of reducing equipment imports, lowering the frame elevation, and prolonging the residence time

Inactive Publication Date: 2008-07-30
CHINA HUANQIU CONTRACTING & ENG CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0002] With the improvement of the performance of polyolefin plastics, the uses are becoming wider and wider, especially the rich raw materials of polypropylene and the wide range of uses, which makes the technology of polypropylene develop rapidly. There are many polypropylene technologies in the world today, mainly divided into gas phase method There are two kinds of polymerization techniques: gas-phase method and liquid-phase method. Each technology has advantages and disadvantages, but there is the disadvantage of uneven residence time of the catalyst in the reactor.
The present invention is based on the liquid-phase propylene polymerization technology. Compared with the loop reactor of liquid-phase propylene bulk polymerization (such as Basell's Spheripol polypropylene technology), it overcomes the disadvantages of relatively high equipment and large floor space when the loop reactor has a large production capacity. The residence time of the polypropylene catalyst in the reactor is different, resulting in uneven particle size of the polypropylene polymer, and the activity of some catalysts moves backward, which affects the product quality.

Method used

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  • Polymerization reactor and method for producing polypropylene by employing the same

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Embodiment 1

[0027] After the catalyst and cocatalyst are mixed in the pre-contact tank, they are added from the nozzle 9 of the first tank reactor, and at the same time, propylene 19 is added and hydrogen 20 or no hydrogen is added as required. In order to prevent the catalyst particles from being broken, a stirrer is used 5 Stir slowly, and control at a lower temperature, the propylene is polymerized on the particles of the catalyst, so that the catalyst is covered with a layer of polymer, providing preparation for the next step of polymerization.

[0028] The pre-polymerized catalyst enters the second tank reactor 1 by gravity flow, and polymer monomer propylene 19 is added in the reactor according to the production polymer ratio, and then hydrogen 20 is added according to the melt index of the produced product, and the hydrogen is used to adjust The molecular weight of the polymer. The catalyst continues to polymerize in the reactor. In order to uniformly remove the heat of reaction ge...

Embodiment 2

[0042] Only change the amount of hydrogen added to: control the hydrogen content of 660ppm.v in the propylene entering each reactor;

Embodiment 3

[0044] Change the amount of hydrogen added to: no addition to the first reactor, and the hydrogen content of the remaining reactors is 900ppm.v;

[0045] Except for the first reactor, for other reactors, ethylene is added to the propylene entering the reactor, and the content is controlled at about 2%.

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Abstract

The invention relates to a polymerization reactor, which is in particular used for producing polypropylene, or used for producing propylene-ethylene random copolymer, propylene-butylene random copolymer or propylene-ethylene-butylene random terpolymer. The polymerization reactor comprises a vessel type reactor (1), a connecting pipe (2), a pressure lifting facility (3), a buffering vessel (15), a carburator (14), a propylene feeding control component (21) and a hydrogen feeding control component (23), the vessel type reactor is provided with a jacket (4), an agitator (5), a cooling water inlet opening (6), a cooling water outlet opening (7), a propylene filling opening (8) and a catalyst filling opening (9), and polymer generated by polyreaction is mixed with a non-polymerized monomer together to be discharged towards downstream through a discharge opening (10). The invention has the advantages that the detention period of the catalyst can tend to be homogeneous, and the particle diameter of the produced polypropylene particles tends to be consistent, etc.

Description

technical field [0001] The present invention relates to a polymerization reactor, especially for producing polypropylene, or for producing propylene-ethylene random copolymer, propylene-butene random copolymer or propylene-ethylene-butene ternary random copolymer thing. Background technique [0002] With the improvement of the performance of polyolefin plastics, the uses are becoming wider and wider. In particular, polypropylene is rich in raw materials and has a wide range of uses, which makes the technology of polypropylene develop rapidly. There are many polypropylene technologies in the world today, mainly divided into gas phase methods There are two kinds of polymerization techniques and liquid phase method, among which gas phase method has multiple polymerization techniques, and liquid phase also has multiple polymerization techniques. Each technique has advantages and disadvantages, but they share the disadvantage of uneven residence time of the catalyst in the reacto...

Claims

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Application Information

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IPC IPC(8): C08F110/06C08F2/01
Inventor 黄新平叶宁
Owner CHINA HUANQIU CONTRACTING & ENG CO LTD
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