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Electrostatic control method for olefin polymerization process

A technology for olefin polymerization and electrostatic control, applied in the field of olefin polymerization, can solve the problems of poor fluidity, residue, loss of liquid-phase antistatic compound, etc., and achieve the effect of reducing surface resistance and low electrostatic voltage

Pending Publication Date: 2022-04-29
ZHEJIANG UNIV HANGZHOU GLOBAL SCI & TECH INNOVATION CENT
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] In the continuous polymerization of olefins, using the above method to directly or indirectly add antistatic compounds to the polymerization reactor can effectively weaken the production of static electricity in the reaction process, but its disadvantage is that the addition of liquid phase antistatic compounds will affect the polymerization reactor. The internal fluid flows and is easily taken out or left on the wall of the reactor during the polymerization reaction, resulting in a certain loss of liquid-phase antistatic compounds
In addition, the high boiling point of the liquid antistatic agent usually prevents it from being vaporized in the polymerization reaction environment, and its poor fluidity also prevents it from being atomized. The antistatic agent that cannot be fully dispersed seriously restricts its antistatic effect.

Method used

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  • Electrostatic control method for olefin polymerization process
  • Electrostatic control method for olefin polymerization process

Examples

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Embodiment 1

[0041] In Example 1, the polymerization was carried out in a polyethylene bubbling fluidized bed using a metallocene catalyst system, and the antistatic compound used was commercially available under the trademark Atmer 163 (formula R-N(CH 2 CH 2 Oh 2 ) 2 The synthetic mixture of alkyldiethanolamine, wherein R is an alkyl group containing 13 to 15 carbon atoms), is transported at the bottom of the bubbling fluidized bed by means of ethylene pneumatic conveying, with a particle size range of 850-1000 μm and a particle size of 850-1000 μm at 60 The nascent polyethylene powder loaded with antistatic compound at °C was left to stand for 60 hours, and the mass ratio of the amount of antistatic compound relative to the polyethylene powder in the bed was the same as Comparative Example 1, which was 0.02% (200ppm). Wherein, the amount of antistatic compound is 4.0% relative to the weight of nascent polyethylene powder used for loading, and the amount of nascent polyethylene powder l...

Embodiment 2

[0049] In Comparative Example 2, the polymerization was carried out in a circulating fluidized bed of polypropylene using a Ziegler-Natta catalyst system, and the antistatic compound used was commercially available under the trademark Atmer 163 (formula R-N(CH 2 CH 2 Oh 2 ) 2 The synthetic mixture of alkyldiethanolamine, wherein R is an alkyl group containing 13 to 15 carbon atoms), adopts the mode of pneumatic conveying of propylene to convey the particle size range of 850-1000 μm in the middle part of the descending section of the circulating fluidized bed and at 60 The nascent polypropylene powder loaded with antistatic compound at °C was left to stand for 72 hours, and the amount of antistatic compound relative to the weight of the polypropylene powder in the bed was the same as that of Comparative Example 2, which was 0.025% (250ppm). Wherein, the amount of antistatic compound is 2.5% relative to the weight of nascent polypropylene powder for loading, and the amount of ...

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Abstract

The invention discloses an olefin polymerization process electrostatic control method which comprises the following steps: mixing nascent state polyolefin powder and an antistatic compound at 30-60 DEG C, and standing for 24-72 hours to obtain nascent state polyolefin powder loaded with the antistatic compound; and when the electrostatic voltage in the olefin polymerization process rises to an electrostatic voltage threshold value, introducing the nascent state polyolefin powder loaded with the antistatic compound into a polymerization reactor filled with polyolefin powder through cascade control so as to control the electrostatic voltage in the olefin polymerization process. According to the method, the dispersion time of the antistatic agent in the gas-phase polymerization reactor can be shortened, and the loss is less, so that the antistatic agent has higher charge elimination effect and stability.

Description

technical field [0001] The invention belongs to the technical field of olefin polymerization, and in particular relates to a method for controlling static electricity in an olefin polymerization process. Background technique [0002] In the industrial production of polyolefins, the dry reaction environment in the gas phase polymerization reactor and the high insulation of polyolefins lead to frequent frictional electrification and slow static dissipation, providing natural conditions for the generation and accumulation of static electricity. The existence of static electricity in the production process may cause potential hazards such as wall sticking and agglomeration, and even cause reactor failure and explosion accidents. Therefore, antistatic agents are widely used in industrial fluidized bed reactors to control static electricity. [0003] The U.S. Patent No. US5034480A discloses a method for preparing ultra-high molecular weight ethylene polymers using an antistatic a...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08F10/00C08F2/34
CPCC08F10/00C08F2/34
Inventor 杨遥范子雄葛世轶黄正梁王靖岱阳永荣
Owner ZHEJIANG UNIV HANGZHOU GLOBAL SCI & TECH INNOVATION CENT
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