Production method of continuous polymerization melt direct spinning functional polyamide fiber and the functional polyamide fiber

A technology of polyamide fiber and production method, which is applied in the field of polymer material synthesis, can solve the problems of difficult to achieve high uniform dispersion of functional powder, poor spinning performance of functional polyamide melt, etc., and achieves large-scale industrialized continuous production, The effect of easy industrialization and improved stability

Active Publication Date: 2021-10-26
CHINESE TEXTILE ACAD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In the process of preparing functional polyamide fibers by masterbatch method, the dispersion of functional powder in high-viscosity polyamide melt mainly depends on the mechanical shear force provided by mixing equipment, so it is difficult to realize the dispersion of functional powder in polyamide melt. The high uniform dispersion in the middle makes the spinning performance of the prepared functional polyamide melt poor

Method used

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  • Production method of continuous polymerization melt direct spinning functional polyamide fiber and the functional polyamide fiber

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0055] (1) The functional powder slurry pre-dispersion made of water, caprolactam and pigment blue 15:3 is continuously transported to the functional powder slurry multi-stage grinding device for grinding and dispersion, in which water, caprolactam and pigment blue 15:3 The mass ratio of the functional powder slurry is 1:0.8:1.8, and the functional powder slurry multi-stage grinding device is composed of 3 grinding machines connected in series to obtain a functional powder with a pigment blue 15:3 content of 50wt% and an average particle size of 0.28μm slurry;

[0056] (2) Mix the functional powder slurry prepared in step (1) with the caprolactam melt and the catalyst through a dynamic mixer, adjust the temperature with a heat exchanger, and then enter the hydrolysis reactor for ring-opening reaction, wherein the catalyst is phosphoric acid, catalyst The addition amount is 400ppm of the mass of the caprolactam melt, the addition amount of the functional powder slurry is 5% of ...

Embodiment 2

[0063] (1) Continuously convey the functional powder slurry pre-dispersion prepared by water, caprolactam and carbon black to the functional powder slurry multi-stage grinding device for grinding and dispersion, wherein the mass ratio of water, caprolactam and carbon black is 1: 0.8:0.77, the functional powder slurry multi-stage grinding device is composed of three grinding machines connected in series to obtain a functional powder slurry with a carbon black content of 30wt% and an average particle size of 0.11 μm;

[0064] (2) Mix the functional powder slurry prepared in step (1) with the caprolactam melt and the catalyst through a dynamic mixer, adjust the temperature with a heat exchanger, and then enter the hydrolysis reactor for ring-opening reaction, wherein the catalyst is phosphoric acid, catalyst The addition amount is 400ppm of the mass of the caprolactam melt, the addition amount of the functional powder slurry is 10.7% of the mass of the caprolactam melt, the temper...

Embodiment 3

[0071] (1) The functional powder slurry pre-dispersion prepared by water, caprolactam and pigment red 179 is continuously transported to the functional powder slurry multi-stage grinding device for grinding and dispersion, wherein the mass ratio of water, caprolactam and pigment red 179 is 1:0.5:0.375, the functional powder slurry multi-stage grinding device is composed of two grinding machines connected in series to obtain a functional powder slurry with a pigment red 179 content of 20wt% and an average particle size of 0.28 μm;

[0072] (2) The functional powder slurry prepared in step (1) is mixed with the caprolactam melt and the catalyst through a dynamic mixer, and the temperature is adjusted by a heat exchanger, and then enters a hydrolysis reactor for ring-opening reaction, wherein the catalyst is metaphosphoric acid, catalyst The addition amount of the caprolactam melt is 1000ppm, the addition amount of the functional powder slurry is 9.4% of the caprolactam melt mass,...

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Abstract

Disclosed are a production method of continuous polymerization melt direct spinning functional polyamide fiber and the functional polyamide fiber. The method comprises: continuously conveying the functional powder slurry pre-dispersion prepared by water, caprolactam and functional powder to a functional powder slurry multi-stage grinding device for grinding and dispersing; the obtained functional powder slurry is mixed with caprolactam melt and The catalyst is mixed evenly by the dynamic mixer, and the temperature is adjusted by the heat exchanger, and then enters the hydrolysis reactor for ring-opening reaction; the obtained functional caprolactam oligomer melt is removed by the oligomer melt dehydrator, and then enters the pre-polymerization reactor for addition polymerization reaction; the obtained functional polyamide prepolymer melt goes through the prepolymer melt dehydrator to remove residual moisture and then enters the post-polymerization reactor for polycondensation reaction; the obtained functional polyamide melt passes through the thin film evaporation system to remove caprolactam monomer It is directly transported to the spinning box for spinning to obtain functional polyamide fibers. The functional powder in the functional polyamide fiber is highly uniformly dispersed.

Description

technical field [0001] The invention relates to the technical field of polymer material synthesis, in particular to a production method of continuous polymerization melt direct spinning functional polyamide fiber and the functional polyamide fiber. Background technique [0002] At present, the preparation method of functional polyamide fiber is mainly the masterbatch method. The masterbatch method is to melt and mix functional powder and carrier resin to obtain functional masterbatch with high functional powder content, and then uniformly mix functional masterbatch melt and polyamide melt to obtain functional polyamide fiber through spinning process. In the process of preparing functional polyamide fibers by masterbatch method, the dispersion of functional powder in high-viscosity polyamide melt mainly depends on the mechanical shear force provided by mixing equipment, so it is difficult to realize the dispersion of functional powder in polyamide melt. The high uniform disp...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): D01F6/90D01F1/10C08G69/16
Inventor 邱志成李鑫曲希明姜锋王雪王颖金剑张厚羽马肖赵亮
Owner CHINESE TEXTILE ACAD
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