Special color master batch for non-woven fabrics, and preparation method thereof
A technology of color masterbatch and non-woven fabric, applied in the field of color masterbatch, can solve the problems of fading of non-woven fiber products, difficult diffusion of fiber products, and easy damage to the quality of non-woven fiber products, etc., and achieves easy diffusion and good light resistance. Effect
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[0031] Example 1, a preparation method of a special color masterbatch for non-woven fabrics, including the following steps: S01: 50 parts by weight of polypropylene resin, 20 parts by weight of macromolecular red, 3 parts by weight of sodium stearate, 4 parts by weight Parts of silica, 2 parts by weight of diphenyl phosphate and 2 parts of stearic acid acyl are added to the mixer and mixed and stirred until the mixing is uniform, wherein the stirring speed in the mixer is 1000 rad / min, and the stirring time is 15 minutes.
[0032] S02: The uniformly stirred raw materials are transported to the screw extruder through an automatic feeder, and the extruded raw materials are extruded through the die hole of the extruder. The setting temperature of the screw extruder is 230°C, The speed of the screw extruder is 800 rad / min.
[0033] S03: The polymer obtained in step S02 is blow-dried and pelletized and then sieved to remove particles that do not meet the particle size requirements, and ...
Example Embodiment
[0035] Example 2, a method for preparing a special color masterbatch for non-woven fabrics, including the following steps: S01: 60 parts by weight of polypropylene resin, 30 parts by weight of macromolecule yellow, 8 parts by weight of magnesium stearate, 6 parts by weight Parts of aluminum silicate, 6 parts by weight of ammonium polyphosphate and 5 parts by weight of n-butyl stearate were added to the mixer and mixed and stirred until the mixture was uniform. The mixing speed in the mixer was 1500 rad / min, and the stirring time was 20min.
[0036] S02: The uniformly stirred raw materials are transported to the screw extruder through an automatic feeder, and the extruded raw materials are extruded through the die hole of the extruder. The setting temperature of the screw extruder is 240°C, The speed of the screw extruder is 1000 rad / min.
[0037] S03: The polymer obtained in step S02 is blow-dried and pelletized and then sieved to remove particles that do not meet the particle siz...
Example Embodiment
[0039] Example 3, a method for preparing a special color masterbatch for non-woven fabrics, including the following steps: S01: Combine 55 parts by weight of polypropylene resin, 25 parts by weight of benzidine yellow G, 5 parts by weight of sodium stearate, and 5 parts by weight. Parts by weight of aluminum silicate, 4 parts by weight of ammonium polyphosphate and 3 parts by weight of oleic acid amide are added to the mixer and mixed and stirred until the mixing is uniform, wherein the stirring speed in the mixer is 1200 rad / min, and the stirring time is 16 min.
[0040] S02: The uniformly stirred raw materials are transported to the screw extruder through an automatic feeder, and the extruded raw materials are extruded through the die hole of the extruder. The setting temperature of the screw extruder is 235°C, The rotation speed of the screw extruder is 900 rad / min.
[0041] S03: The polymer obtained in step S02 is blow-dried and pelletized and then sieved to remove particles th...
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