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
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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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