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Method for continuously synthesizing epichlorohydrin rubber by using kneading reactor

A chlorohydrin rubber and reactor technology, applied in the field of rubber manufacturing, can solve the problems of wide molecular weight distribution of rubber, difficult to control polymerization temperature, low stirring and mixing efficiency, etc., to achieve good product quality, reduce cleaning and wall-hanging glue, and raw material utilization. high rate effect

Active Publication Date: 2021-01-15
WUHAN YOUJI IND
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0013] In order to overcome the existing solution polymerization method for synthesizing chlorohydrin rubber, the stirring and mixing efficiency of the tank reactor is low, the reaction time is long, the temperature rise of the polymerization is too large, and the polymerization The temperature is difficult to control, the molecular weight distribution of the rubber is wide, and the performance is unstable. The present invention proposes a method for continuously synthesizing chlorohydrin rubber using a kneading reactor.

Method used

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  • Method for continuously synthesizing epichlorohydrin rubber by using kneading reactor
  • Method for continuously synthesizing epichlorohydrin rubber by using kneading reactor

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Embodiment 1

[0060] Embodiment 1 of the present invention provides a method for continuously synthesizing epichlorohydrin rubber using a kneading reactor, comprising the following steps:

[0061] S1, after the pretreatment of the kneading reactor with vacuum treatment and sufficient nitrogen replacement, the refined qualified toluene and epichlorohydrin are put into the pretreated kneading reactor at a ratio of volume to mass ratio of 5L: 1Kg, and the stirring process is started , the control feed temperature is 50 ℃, then, drop into the catalyst of monomer mass 2% (the mass ratio of triisobutylaluminum, phosphoric acid and aniline is 90:180:18), control the polymerization reaction system in the kneading reactor The concentration of the compound is 20%. The material is continuously added to the kneading reactor through the feeding pump, and the material is continuously discharged to carry out the process of continuous feeding-continuous polymerization reaction (the continuous polymerization...

Embodiment 2

[0067] Embodiment 2 of the present invention provides a method for continuously synthesizing epichlorohydrin rubber using a kneading reactor, comprising the following steps:

[0068]S1, after the pretreatment of the kneading reactor with vacuum treatment and sufficient nitrogen replacement, the refined qualified toluene and mixed monomers (epichlorohydrin and ethylene oxide with a mass ratio of 1:1) were mixed in a volume-to-mass ratio of 5.5L : the ratio of 1Kg is put into the kneading reactor after the pretreatment, and the stirring process is started, and the control feeding temperature is 60°C, and then, the catalyst (the mass ratio of triisobutylaluminum, phosphoric acid and aniline of 2% of monomer mass) is dropped into 100:160:20), the concentration of the polymerization reaction system in the kneading reactor is controlled to be 15%, and the materials are continuously added to the kneading reactor through the feed pump, and the materials are continuously discharged, and...

Embodiment 3

[0073] Embodiment 3 of the present invention provides a method for continuously synthesizing epichlorohydrin rubber using a kneading reactor, comprising the following steps:

[0074] S1, after the pretreatment of vacuum treatment and nitrogen full replacement to the kneading reactor, the refined qualified toluene and mixed monomers (epichlorohydrin and propylene oxide with a mass ratio of 2:1) are 5.3L by volume and mass: The ratio of 1Kg is put into the kneading reactor after the pretreatment, and the stirring process is started, and the feeding temperature is controlled to be 70°C, and then, the catalyst (the mass ratio of triisobutylaluminum, phosphoric acid and aniline is 100% by mass) is dropped into 2% of the monomer mass. : 200: 16), controlling the concentration of the polymerization reaction system in the kneading reactor to be 10%, continuously adding materials to the kneading reactor through the feeding pump, continuously discharging, and carrying out the process of ...

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Abstract

The invention provides a method for continuously synthesizing epichlorohydrin rubber by using a kneading reactor. The method comprises the following steps of: sequentially adding a predetermined amount of toluene, a monomer and a catalyst into a kneading reactor, starting stirring, heating to start a reaction, continuously adding materials into the kneading reactor through a feeding pump accordingto a set feeding ratio, continuously discharging, preparing a glue solution by adopting a process of material and catalyst feeding at a medium temperature, continuous feeding and continuous polymerization reaction, carrying out devolatilization treatment, sending the devolatilized rubber solution to a gel kettle for gelling to obtain rubber particles, removing surface water from the rubber particles through a vibrating screen, drying the rubber particles in an oven, carrying out extrusion molding on the dried raw rubber, metering and packaging the raw rubber, and carrying out post-treatment to obtain the epichlorohydrin rubber. The kneading reactor is used for continuously synthesizing the epichlorohydrin rubber, the working volume and the heat transfer area are large, the heat transfer surface has a self-descaling function, and the method has the advantages of being high in mass transfer rate, simple in reaction operation, few in side reaction, high in raw material utilization rate and good in product quality.

Description

technical field [0001] The invention relates to the field of rubber manufacture, in particular to a method for continuously synthesizing epichlorohydrin rubber by using a kneading reactor. Background technique [0002] Epichlorohydrin rubber (also known as epichlorohydrin rubber, epichlorohydrin rubber or epichlorohydrin rubber) is made of polymer grade epichlorohydrin (or a mixture of comonomers such as ethylene oxide) in the presence of triisobutyl aluminum It is made by polymerization in toluene solution in the presence of a catalyst as the main component. Chlorohydrin rubber has excellent oil resistance, solvent resistance, acid resistance, alkali resistance, weather resistance and ozone resistance, its gas permeability resistance is the lowest among all rubber types, and its shock absorption performance and high and low temperature resistance are outstanding. It can work at 120°C for a long time, and its low temperature resistance can reach -30°C. In addition, it also ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C08G65/24C08G65/08C08G65/06C08G65/12B01J19/18
CPCC08G65/24C08G65/08C08G65/06C08G65/12B01J19/18
Inventor 舒振操孙波程娟聂少春周峰袁鹏朱明伟黄正望毛利民
Owner WUHAN YOUJI IND
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