Method of continuously preparing poly terephthaloyl-p-phenylene diamine fibre
A poly(p-phenylene terephthalamide) and fiber technology, which is applied in the field of continuous preparation of poly(p-phenylene terephthalamide) fibers, can solve the problems of long dissolution time, unfavorable industrial production, and difficult stirring, etc. Achieve the effect of improving mixing uniformity, good self-cleaning effect and high mixing uniformity
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Embodiment 1
[0019] 100% concentrated sulfuric acid and poly-p-phenylene terephthalamide (PPTA) powder were added at a rate of 71.08g / min and 16.6g / min by using a liquid metering feeding system and a high-precision weight-loss continuous metering electronic scale. Φ40, length-to-diameter ratio of 15, counter-rotating, rotating speed of 200rpm in the first twin-screw extruder, after thorough mixing, continuously enter the second twin-screw extruder with diameter of 55mm, length-diameter ratio of 60, rotating speed of 40rpm In the extruder, control the screw temperature of the first twin-screw extruder and the second twin-screw extruder to be 85°C, and continuously extrude the spinning solution that is fully mixed, the temperature is well adjusted, and the bubbles are completely removed. After metering, After filtering, it is sent to the spinneret, and the size of the spinneret cap is Φ0.06×300 holes, and enters the coagulation bath spinning tube through the 5cm air gap layer. The coagulation...
Embodiment 2
[0021] 99% concentrated sulfuric acid and poly-p-phenylene terephthalamide (PPTA) powder were added at a rate of 71.08g / min and 16.6g / min to the Φ25, length-to-diameter ratio of 8, co-rotating in the first twin-screw extruder with a speed of 150rpm, after being fully mixed, it continuously enters the second twin-screw extruder with a diameter of 25mm, a length-to-diameter ratio of 30, and a speed of 200rpm In the extruder, control the screw temperature of the first twin-screw extruder and the second twin-screw extruder to be 50°C, and continuously extrude the spinning solution that is fully mixed, the temperature is well adjusted, and the bubbles are completely removed. After metering, After filtering, it is sent to the spinneret, the size of the spinneret cap is Φ0.06×300 holes, and it enters the coagulation bath spinning tube through the air gap layer of 5cm. The temperature of the coagulation bath is 5°C, and the spinning speed is 120m / min. The nozzle is stretched 6 times, ...
Embodiment 3
[0023] 98% concentrated sulfuric acid and poly-p-phenylene terephthalamide (PPTA) powder were added at a rate of 70.08g / min and 20.6g / min to the Φ90, length-to-diameter ratio of 20, counter-rotating, rotating speed of 300rpm in the first twin-screw extruder, after thorough mixing, continuously enter the second twin-screw extruder with diameter of 145mm, length-diameter ratio of 60, rotating speed of 10rpm In the extruder, control the screw temperature of the first twin-screw extruder and the second twin-screw extruder to be 100°C, and continuously extrude the spinning solution that is fully mixed, the temperature is well adjusted, and the bubbles are completely removed. After filtering, it is sent to the spinneret, the size of the spinneret cap is Φ0.06×300 holes, and it enters the coagulation bath spinning tube through the air gap layer of 5cm. The temperature of the coagulation bath is 5°C, and the spinning speed is 120m / min. The nozzle is stretched 6 times, the spun tow is ...
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