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
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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
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