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Method for continuous production of polyamide functional masterbatch and polyamide functional masterbatch

A technology of functional masterbatch and polyamide, which is applied in the continuous production of polyamide functional masterbatch and polyamide functional masterbatch. It can solve the problems of uniform dispersion of difficult functional powder and difficult application of functional masterbatch, so as to reduce the water content. , improved production efficiency, and ease of industrial implementation

Active Publication Date: 2019-06-07
CHINESE TEXTILE ACAD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Since in the melt blending method, the dispersion of the functional powder in the high-viscosity carrier resin melt mainly depends on the mechanical shear force provided by the mixing equipment, it is difficult to realize the functional powder in the carrier resin melt at a small scale height. Uniform dispersion, which makes it difficult for the functional masterbatch prepared by the melt blending method to be suitable for the preparation of fine denier or ultrafine denier functional fibers

Method used

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  • Method for continuous production of polyamide functional masterbatch and polyamide functional masterbatch
  • Method for continuous production of polyamide functional masterbatch and polyamide functional masterbatch
  • Method for continuous production of polyamide functional masterbatch and polyamide functional masterbatch

Examples

Experimental program
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Effect test

Embodiment 1

[0051] (1) The functional powder slurry pre-dispersion prepared by water, caprolactam and pigment blue 15:3 is continuously transported to the functional powder slurry multi-stage grinding device for grinding and dispersion, wherein water, caprolactam and pigment blue 15:3 The mass ratio 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;

[0052] (2) The functional powder slurry prepared in step (1) is mixed with the caprolactam melt and the catalyst through a dynamic mixer, and after the temperature is adjusted by a heat exchanger, it enters a high-pressure hydrolysis reactor for ring-opening reaction, wherein the catalyst is phosphoric acid, catalyst The addition amount of the caprolactam melt is 90ppm, the addition amount of the functional powder slurry is 78% of the caprolactam ...

Embodiment 2

[0057] (1) The functional powder slurry pre-dispersion prepared by water, caprolactam and carbon black is continuously transported 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: 0.8:1.2, 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 40wt% and an average particle size of 0.15 μm.

[0058] (2) The functional powder slurry prepared in step (1) is mixed with the caprolactam melt and the catalyst through a dynamic mixer, and after the temperature is adjusted by a heat exchanger, it enters a high-pressure hydrolysis reactor for ring-opening reaction, wherein the catalyst is phosphoric acid, catalyst The addition amount of the caprolactam melt is 500ppm, the addition amount of the functional powder slurry is 75% of the caprolactam melt mass,...

Embodiment 3

[0063] (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 1:1:3, the functional powder slurry multi-stage grinding device is composed of 5 grinding machines connected in series to obtain a functional powder slurry with a pigment red 179 content of 60wt% and an average particle size of 0.24μm;

[0064] (2) The functional powder slurry prepared in step (1) is mixed with the caprolactam melt and the catalyst through a dynamic mixer, and after the temperature is adjusted by a heat exchanger, it enters a high-pressure hydrolysis reactor for ring-opening reaction, wherein the catalyst is metaphosphoric acid, The amount of catalyst added is 1500ppm of the mass of caprolactam melt, the amount of functional powder slurry added is 250% of the mass of caprolac...

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Abstract

The invention discloses a method for continuous production of a polyamide functional masterbatch and the polyamide functional masterbatch. The method comprises the following steps: continuously conveying a functional powder slurry predispersion prepared from water, caprolactam and a functional powder to a functional powder slurry multi-stage grinding device for grinding and dispersing; uniformly mixing an obtained functional powder slurry with a caprolactam melt and a catalyst through a dynamic mixer, adjusting the temperature of an obtained mixture through a heat exchanger, and allowing the mixture to enter a high-pressure hydrolysis reactor for a ring-opening reaction; removing excess water from an obtained functional masterbatch oligomer oligomeric melt through an oligomer melt dehydrator, and allowing an obtained product to enter a normal-pressure polymerization reactor for a polymerization reaction; and removing a caprolactam monomer from an obtained polyamide functional masterbatch melt through a film evaporation devolatilization system, and directly carrying out pelletization molding so as to obtain the polyamide functional masterbatch. The functional powder in the polyamidefunctional masterbatch continuously produced by using the method provided by the invention is dispersed in a highly uniform manner, so the polyamide functional masterbatch provided by the invention is applicable to production of products like high-quality fibers and films.

Description

technical field [0001] The invention relates to the technical field of polymer material synthesis, in particular to a method for continuously producing polyamide functional master batches and the polyamide functional master batches. Background technique [0002] At present, the preparation method of polyamide functional masterbatch is mainly the pre-spinning coloring method of functional masterbatch. Functional masterbatch is an aggregate prepared by uniformly loading super-normal pigments or dyes in resin. The preparation of functional masterbatch usually adopts the melt blending method, and the carrier resin and functional powder are uniformly mixed above the viscous flow temperature of the carrier resin, relying on the strong shear force provided by the mixing equipment, so that the functional powder can be stabilized with a certain particle size. , Evenly dispersed in the carrier resin. Since in the melt blending method, the dispersion of the functional powder in the h...

Claims

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Application Information

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IPC IPC(8): C08J3/22C08G69/16C08G69/46B29B9/06
Inventor 邱志成李鑫姜锋张厚羽王雪曲希明王颖盛平厚金剑赵亮
Owner CHINESE TEXTILE ACAD
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