Method of continuously preparing poly terephthaloyl-p-phenylene diamine fibre

A technology of poly-p-phenylene terephthalamide and poly-p-phenylene terephthalamide, which is applied in the field of continuous preparation of poly-p-phenylene terephthalamide fiber, can solve the problem of long dissolution time and unfavorable industrial Production, mixing difficulties and other problems, to achieve high mixing uniformity, improve production efficiency, and short defoaming time

Inactive Publication Date: 2005-11-09
DONGHUA UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] In the early 1970s, Yumi was DuPont who first invented PPTA / H 2 SO 4 The method of dry spraying-wet spinning of liquid crystal solution has produced this kind of high-strength and high-modulus PPTA fiber, but there are still PPTA / H 2 SO 4 In the preparation process of the spinning liquid crystal solution, the stirring and defoaming of the high-viscosity solution are difficult technical problems. Usually, the PPTA resin is dissolved in 99-100% sulfuric acid at 80-90°C, and it takes at least 3 hours, while PPTA / H 2 SO 4 The defoaming of spinning liquid crystal solution often takes longer time, up to tens of hours to dozens of hours, which is not only unfavorable for continuous industrial production, but also PPTA is prone to degradation during the long-term dissolution and defoaming process, thus affecting Strength of PPTA fiber
[0004] Chinese invention patent 200310109240 discloses a semi-continuous method for preparing poly(p-phenylene terephthalamide) fibers, adding poly(p-phenylene terephthalamide) resin and concentrated sulfuric acid into a mixing cylinder and mixing them with twin-screw The extruder solves the problems of long dissolving time of poly-p-phenylene terephthalamide resin in concentrated sulfuric acid and difficult defoaming of spinning solution, but for industrial production, there are still difficulties in stirring during the mixing process and Difficult to mix evenly

Method used

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Examples

Experimental program
Comparison scheme
Effect test

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 twin-screw extruder 1 with a speed of 200rpm, after being fully mixed, continuously enter a twin-screw extruder with a diameter of 55mm, a length-to-diameter ratio of 60, and a speed of 40rpm In 2, control the screw temperature of twin-screw extruders 1 and 2 to be 85°C, continuously extrude the spinning solution that is fully mixed, the temperature is adjusted, and the bubbles are completely removed. After metering and filtering, it is sent to the spinneret. The size of the spinneret is Φ0.06×300 holes. It enters the coagulation bath spinning tube through the 5cm air gap layer. The coagulation bath temperature is 5°C, the spinning speed is 120m / min, and the nozzle is stretched...

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 twin-screw extruder 1 with a speed of 150rpm, after being fully mixed, continuously enter a twin-screw extruder with a diameter of 25mm, a length-to-diameter ratio of 30, and a speed of 200rpm In 2, control the screw temperature of twin-screw extruders 1 and 2 to be 50°C, continuously extrude the spinning solution that is fully mixed, the temperature is adjusted, and the bubbles are completely removed. After metering and filtering, it is sent to the spinneret. The size of the spinneret is Φ0.06×300 holes. It enters the coagulation bath spinning tube through the 5cm air gap layer. The coagulation bath temperature is 5°C, the spinning speed is 120m / min, and the nozzle is stretched 6 times. After the tow is washed and neutralized, it is sent to the heat treatment device, heat treated at 400...

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 by using a liquid metering feeding system and a high-precision weight-loss continuous metering electronic scale respectively. Φ90, length-to-diameter ratio of 20, counter-rotating twin-screw extruder 1 with a speed of 300rpm, after being fully mixed, it continuously enters a twin-screw extruder with a diameter of 145mm, a length-to-diameter ratio of 60, and a speed of 10rpm In 2, control the screw temperature of twin-screw extruders 1 and 2 to be 100°C, continuously extrude the spinning solution that is fully mixed, the temperature is adjusted, and the bubbles are completely removed. After metering and filtering, it is sent to the spinneret. The size of the spinneret is Φ0.06×300 holes. It enters the coagulation bath spinning tube through the 5cm air gap layer. The coagulation bath temperature is 5°C, the spinning speed is 120m / min, and the n...

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Abstract

The invention discloses a method for continuously preparing p-phenylene terephthalamide (PPTA) fiber, including the steps of: (1) continuously adding 98-100% oil of vitriol and PPTA with specific logarithmic viscosity of 4.0-8.5 dl / g to an double spiral extruder, where the weight percent of PPTA is 14-24% and the mixing temperature is 50-100 deg.C; (2) fully mixing and entering in the other extruder, where the adjusting temperature is 50-100 deg.C and the staying time is 10-60 min, fully mixing, adjusting temperature and defoaming and then extruding them; (3) after measuring and filtering spinning solution, obtaining the invention by the routine steps, such as dry spraying-wet spinning. The advantages are short time for mixing materials, adjusting temperature and defoaming high mixing uniformity of materials able to implement continuous, stable filature in a short time, raising the production efficiency.

Description

technical field [0001] The invention designs a method for preparing fibers, in particular relates to a method for continuously preparing poly(p-phenylene terephthalamide) fibers Background technique [0002] As we all know, poly-p-phenylene terephthalamide fiber is a typical aromatic polyamide fiber, also known as aramid 1414 or PPTA fiber, which has excellent properties such as high strength, high modulus, and high temperature resistance. The fastest-growing high-tech fiber in fiber materials is mainly used in industrial textiles, especially in the occasions where many products require lightweight and high performance, only polyparaphenylene terephthalamide (PPTA) can be used. )fiber. [0003] In the early 1970s, Yumi was DuPont who first invented PPTA / H 2 SO 4 The method of dry spraying-wet spinning of liquid crystal solution has produced this kind of high-strength and high-modulus PPTA fiber, but there are still PPTA / H 2 SO 4 In the preparation process of the spinnin...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): D01D1/00
Inventor 刘兆峰尤秀兰陈蕾潘婉莲胡祖明
Owner DONGHUA UNIV
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