High-performance light-storing noctilucent master batch for polyolefin plastic and preparation method thereof
A high-performance, polyolefin technology, applied in the field of plastic product coloring, can solve the problems of low concentration of luminous powder, easy darkening of masterbatch color, unsatisfactory dispersion performance, etc., to achieve good luminous effect, pure color and dispersibility Good results
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Embodiment 1
[0010] LLDPE (melt flow rate is 15-25g / 10min; particle size is 30-60 mesh) 15%; LDPE (melt flow rate is 5-10g / 10min; particle size is 50-100 mesh) 21.5%; one (or Various) luminous pigment 60%; polyethylene wax (molecular weight 3000-4000) 3.0%; bisethylene stearamide 1.5%. Put 60% of the total amount of the above-mentioned luminous pigments into a plastic or ceramic mixer and mix evenly with other components, and use a twin-screw extruder for melt blending. The temperature is controlled at 140-180 ° C, and the remaining 40 % of the luminous pigment is evenly metered into the barrel of the extruder through side feeding, mixed and extruded together with the main material, and then granulated by water-cooled cutting of the strands or air-cooled cutting of the die surface. , and finally dried to obtain the masterbatch of the present invention, the degree of dispersion is 2.
Embodiment 2
[0012] LLDPE (melt flow rate is 15-25g / 10min; particle size is 30-60 mesh) 10%; LDPE (melt flow rate is 5-10g / 10min; particle size is 50-100 mesh) 27.5%; one (or Various) luminous pigment 60%; polyethylene wax (molecular weight 3000-4000) 2%; bisethylene stearamide 0.5%. Put 60% of the total amount of the above-mentioned luminous pigments into a plastic or ceramic mixer and mix evenly with other components, and use a twin-screw extruder for melt blending. The temperature is controlled at 140-180 ° C, and the remaining 40 % of the luminous pigment is evenly metered into the barrel of the extruder through side feeding, mixed and extruded together with the main material, and then granulated by water-cooled cutting of the strands or air-cooled cutting of the die surface. , and finally dried to obtain the masterbatch of the present invention, the degree of dispersion is 3.
Embodiment 3
[0014] LLDPE (melt flow rate is 15-25g / 10min, particle size is 30-60 mesh) 15.5%; LDPE (melt flow rate is 5-10g / 10min; particle size is 50-100 mesh) 20%; one (or more) species) luminous pigment 62%; polyethylene wax (molecular weight 3000-4000) 2%; bisethylene stearamide 0.5%. Put 60% of the total amount of the above-mentioned luminous pigments into a plastic or ceramic mixer and mix evenly with other components, and use a twin-screw extruder for melt blending. The temperature is controlled at 140-180 ° C, and the remaining 40 % of the luminous pigment is evenly metered into the barrel of the extruder through side feeding, mixed and extruded together with the main material, and then granulated by water-cooled cutting of the strands or air-cooled cutting of the die surface. , and finally dried to obtain the masterbatch of the present invention, the degree of dispersion is 3.
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