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Method for Rapid Establishment of Ethylene Polymerization/Copolymerization in Gas Phase Fluidized Bed Reactor

A gas-phase fluidized bed and ethylene polymerization technology, which is applied in the field of conventional chromium-based catalysts to catalyze ethylene polymerization/copolymerization to prepare corresponding polymers, can solve the problems of re-stopping and changing beds, affecting product quality, and difficulty in establishing reactions. The effect of short switching time, low price, and simple operation process

Active Publication Date: 2020-05-08
PETROCHINA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method has the following problems: the method uses a metallocene catalyst to initiate polymerization, but the metallocene catalyst and the conventional chromium-based catalyst are poisonous to each other, and the metallocene replacement does not cut the bottom during the switching process of the catalyst. It is difficult to establish a reaction, and the consequences are to affect the quality of subsequent products and produce a large amount of transitional materials. In severe cases, it is only possible to stop the machine and change the bed
Due to the control characteristics of the fluidized bed reactor, the fluctuation of the reaction temperature will cause large static electricity and severe flakes, which will eventually lead to the shutdown of the device

Method used

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  • Method for Rapid Establishment of Ethylene Polymerization/Copolymerization in Gas Phase Fluidized Bed Reactor
  • Method for Rapid Establishment of Ethylene Polymerization/Copolymerization in Gas Phase Fluidized Bed Reactor

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Effect test

Embodiment 1

[0047] A method for quickly establishing ethylene polymerization / copolymerization in a 50kg / hr gas-phase fluidized-bed reactor, comprising the following steps:

[0048] After filling 100kg of suitable seed bed into the reactor, after introducing nitrogen to replace the trace amount of water and oxygen in the reaction system, switch to ethylene, hydrogen, comonomer and other circulating gases to adjust the composition, and then add 0.01kg of organic The chromium-based S-2 type catalyst initiates the establishment of the polymerization reaction, and then switches to a conventional chromium-based catalyst, and at the same time stops adding the organic chromium-based S-2 type catalyst, and uses a conventional chromium-based catalyst to catalyze ethylene polymerization / copolymerization to produce the corresponding polymer.

[0049] ① replacement

[0050] a. Nitrogen replacement

[0051] After the bed is installed, control the nitrogen pressure to 0.7MPa, and after 10-20 times of p...

Embodiment 2

[0068] A method for quickly establishing ethylene polymerization / copolymerization in a 50kg / hr gas-phase fluidized-bed reactor, comprising the following steps:

[0069] After filling 100kg of suitable seed bed into the reactor, after introducing nitrogen to replace the trace amount of water and oxygen in the reaction system, switch to ethylene, hydrogen, comonomer and other circulating gases to adjust the composition, and then add 0.01kg of organic The chromium-based S-2 type catalyst initiates the establishment of the polymerization reaction, and then switches to a conventional chromium-based catalyst, and at the same time stops adding the organic chromium-based S-2 type catalyst, and uses a conventional chromium-based catalyst to catalyze ethylene polymerization / copolymerization to produce the corresponding polymer.

[0070] ① replacement

[0071] a. Nitrogen replacement

[0072] After the bed is installed, control the nitrogen pressure to 0.7MPa, and after 10-20 pressure r...

Embodiment 3

[0089] A method for quickly establishing ethylene polymerization / copolymerization in a 50kg / hr gas-phase fluidized-bed reactor, comprising the following steps:

[0090] After filling 100kg of suitable seed beds into the reactor, after introducing nitrogen to replace the trace amount of water and oxygen in the reaction system, switch to circulating gases such as ethylene, hydrogen, and comonomers to adjust the composition, and then add 0.05kg of organic The chromium-based S-2 catalyst initiates the establishment of a polymerization reaction, and then switches to a conventional chromium-based catalyst, while stopping the addition of an organic chromium-based S-2 catalyst, and uses a conventional chromium-based catalyst to catalyze ethylene polymerization / copolymerization to produce the corresponding polymer.

[0091] ① replacement

[0092] a. Nitrogen replacement

[0093] After the bed is installed, control the nitrogen pressure to 0.7MPa, and after 10-20 times of pressure repl...

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Abstract

The invention discloses a method for quickly building ethylene polymerization / copolymerization reaction in a gas phase fluidized bed reactor. The method is characterized by comprising the following steps: after a proper seed bed is filled, feeding nitrogen to replace trace water oxygen in a reaction system, switching into ethylene, hydrogen and copolymerization monomers for component adjustment, then initiating polymerization reaction by adopting an organic chromium family S-2 type catalyst, switching into a conventional chromium family catalyst, stopping adding the organic chromium family S-2type catalyst at the same time, and carrying out catalytic ethylene polymerization / copolymerization by adopting the conventional chromium family catalyst to produce a corresponding polymer. The invention provides a method for quickly building polymerization reaction in an ethylene polymerization / copolymerization gas phase fluidized bed reactor, and in the method, change of polymerization reactionparameters is not needed, the seed bed does not need to be switched, and a small quantity of raw materials are used and the energy consumption is low during replacement of the reaction system, so that production accidents such as sheeting of the reaction system, big static electricity of a polymerization device, high content of polymer fine powder, equipment shutdown and the like are avoided, andthe production period is shortened.

Description

technical field [0001] The invention is a method for rapidly establishing ethylene polymerization / copolymerization reaction in a gas-phase fluidized bed reactor. It belongs to the preparation method of polyethylene. It particularly relates to a method for preparing corresponding polymers by catalyzing ethylene polymerization / copolymerization with conventional chromium series catalysts. Background technique [0002] The gas phase polyethylene process has the advantages of short process, small equipment footprint, low equipment investment, mild operating conditions, production unit consumption and low environmental pollution. Therefore, it was developed in the 1970s and after 30 years of rapid development. It has become the mainstream of polyethylene production technology. At present, the relatively advanced and mature full-density gas-phase process in the world mainly includes the Uniopl process of Univation Company, the Innovene G process of Ineos Company, the Spherilene p...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C08F10/02C08F4/69C08F2/34
CPCC08F10/02C08F4/69C08F2/34
Inventor 王登飞郭峰杜威高宇新赵成才宋磊王斯晗姜进宪付义赵增辉任合刚王立娟何书艳张瑀健国海峰李瑞孙彬彬王熺王立明闫磊磊何贵磊李洪兴郭常辉
Owner PETROCHINA CO LTD
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