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Post-treatment method for polysulfone resin prepared by solution method

A polysulfone and solution method technology, applied in the post-processing field of polysulfone resin, can solve the problems of reducing recovery rate, difficult separation, low powder density, etc., to reduce energy consumption and cost, reduce washing times, and reduce bulk density. improved effect

Inactive Publication Date: 2012-07-25
KINGFA SCI & TECH CO LTD +2
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

But this method also has some problems and deficiencies, for example: pulverized smaller particle size solids tend to block and pass through the mesh or sieve, causing separation difficulties and greater losses during solid-liquid separation, reducing the Recovery rate; although the resin is a fine particle or powder, its microstructure is still dense, and it still needs to consume a large amount of washing solvent during washing and can be purified after repeated washing. The production cost is high and the efficiency is low; the powder resin is directly extruded into pellets Feeding is difficult during extrusion modification; the powder after drying has a very small density, which is easy to raise dust and pollute the environment; once dust or other dirt is mixed in, it is difficult to clean up; the bulk density is small, and it takes up a lot of space during storage and transportation, so it has to be cleaned again. Post-processing such as compaction

Method used

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  • Post-treatment method for polysulfone resin prepared by solution method
  • Post-treatment method for polysulfone resin prepared by solution method

Examples

Experimental program
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Effect test

Embodiment 1

[0031] In a 50L reactor, 15.78kg of polyethersulfone resin was prepared by using 36.81kg of sulfolane as a solvent. The solid content in the resin solution was 30%. There are 10 spray holes evenly distributed, and the aperture of each hole is 5.0mm. The resin solution is extruded from the spray holes to form a thin stream. The extrusion speed is 4.8m / min. The thin stream first enters the sulfolane concentration of 65% by mass. In the first-stage coagulation bath of sulfolane aqueous solution at a temperature of 95°C, the length of the coagulation bath is 1.5m, the draft ratio is 3.0, and the filaments are driven by guide rollers before entering the sulfolane aqueous solution with a sulfolane concentration of 20% by mass and a temperature of 80°C In the second-stage coagulation bath, the length of the coagulation bath is 1.5m, and the drafting ratio is 1.8. After leaving the bath, the stretching ratio of the drafting roller is 1.2 for further stretching, and finally enters the p...

Embodiment 2

[0035] Use 40.84kg sulfolane in a 50L reactor to prepare 13.61kg of polybiphenyl ether sulfone resin with a solid content of 25%, and pressurize the reactor with high-purity nitrogen so that the pressure in the system is 0.3MPa, and the bottom of the reactor is uniform There are 10 spray holes distributed, and the aperture of each hole is 8.5mm. The resin solution is extruded from the spray holes to form a thin flow. The extrusion speed is 7.5m / min. The thin flow first enters the sulfolane concentration of 75% by mass, and the temperature In the first-stage coagulation bath of sulfolane aqueous solution at 110°C, the length of the coagulation bath is 1.5m, the draft ratio is 3.5, the filaments are driven by guide rollers and then enter the sulfolane aqueous solution with a concentration of sulfolane of 35% by mass and a temperature of 90°C. In the second stage coagulation bath, the length of the coagulation bath is 1.5m, and the draft ratio is 1.5. 1.2. After leaving the bath,...

Embodiment 3

[0039] In a 50L reactor, use 36.8kg of dimethyl sulfoxide as a solvent to prepare 15.8kg of polysulfone resin with a solid content of 30%, and pressurize the reactor with high-purity nitrogen so that the pressure in the system is 0.3MPa. There are 20 nozzle holes evenly distributed, and the diameter of each hole is 2.0mm. The resin solution is extruded from the nozzle holes to form a thin stream. The extrusion speed is 5.5m / min. The thin stream first enters the dimethyl sulfoxide concentration of 85% by mass, in the first-stage coagulation bath of dimethyl sulfoxide aqueous solution at a temperature of 90°C, the length of the coagulation bath is 1.5m, the draft ratio is 2.7, and the filaments are driven by guide rollers and then enter the concentration of dimethyl sulfoxide In the second coagulation bath of dimethyl sulfoxide aqueous solution with a temperature of 50% by mass and a temperature of 70°C, the length of the coagulation bath is 1.5m, the draft ratio is 1.9, and the ...

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Abstract

The invention discloses a post-treatment method for polysulfone resin prepared by a solution method. The post-treatment method comprises the following steps that: (1) inert gas is filled into a reaction kettle to make the pressure inside the reaction kettle higher than the atmosphere pressure, and then is extruded out from nozzle holes in the lower part of the reaction kettle to form resin flow; (2) the resin flow enters coagulating batch through a drawing roller and coagulates while drawing in the coagulating batch under the action of the drawing roller to form threads; (3) the threads enter a granulator through a driving roller to be cut into resin particles; and (4) the resin particles are washed, cleaned and dried to form pure resin particles. According to the post-treatment method, the washing times can be reduced in the washing process, i.e. the post-treatment method can conform to the qualification standard, so that the energy consumption and cost are reduced. Meanwhile, according to the post-treatment method, the loss of the polysulfone resin in the post-treatment process is reduced, and the yield is increased, so that the packing density of the pure resin is greatly improved, and the resin particles obtained by the post-treatment can be directly used for injection, extrusion molding or modification.

Description

technical field [0001] The invention belongs to the field of preparation of special engineering plastics, and in particular relates to a post-treatment method of polysulfone resin prepared by a solution method. Background technique [0002] The traditional industrial post-treatment process for special engineering plastics such as polyethersulfone resins is to crush them into powder or small granular solids with a crusher, and then use a large amount of water or other solvents to cook at high temperature for many times, so that the solvent and The by-product inorganic salt is dissolved in the washing liquid, and then the solid-liquid separation is carried out by means of centrifugation or pressure filtration to achieve the purpose of purifying the resin. It is generally believed that the smaller the particle size of the solid material, the easier it is to remove impurities such as solvents and by-product inorganic salts. But this method also has some problems and deficiencie...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B29B9/06
Inventor 代惊奇曾祥斌曹民饶先花苏成晓吴浩斌叶南飚宁凯军
Owner KINGFA SCI & TECH CO LTD