Flame retardant polyphenylene oxide composition and preparation method thereof
A technology of polyphenylene ether and composition, applied in the field of flame retardant polyphenylene ether composition, can solve the problems of low heat resistance grade, rigidity of polyphenylene ether, loss of heat resistance, low flame retardant effect, etc. The effect of stable quality, easy processing and high production efficiency
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Embodiment 1
[0033] 55% by weight of polyphenylene ether resin (intrinsic viscosity of 0.35 dL / g), 30% by weight of high impact polystyrene resin (HIPS), 9% by weight of elastomer SBS, 5% by weight of brominated epoxy resin Resin flame retardant and 1% by weight of antioxidant β-(3,5-di-tert-butyl-4-hydroxyphenyl) octadecyl propionate were stirred in a high-speed mixer for 5 minutes, and after mixing uniformly, Put into twin-screw extruder for extrusion and granulation. The length-diameter ratio of the twin-screw extrusion equipment is 35, the control feeding speed is 8rpm / min, the screw speed is 200rpm / min, and the temperature of each zone of the screw barrel is 200°C for the first stage, 245°C for the second stage, and 245°C for the third stage. ℃, the fourth section is 245℃, the fifth section is 245℃, the sixth section is 245℃, the seventh section is 245℃, the eighth section is 245℃, the ninth section is 245℃, and the die temperature is 245℃.
Embodiment 2
[0035]55% by weight of polyphenylene ether resin (intrinsic viscosity of 0.35 dL / g), 27% by weight of high impact polystyrene resin (HIPS), 9% by weight of elastomer SBS, 5% by weight of brominated epoxy resin Resin-based flame retardant, 3.3 wt% compatibilizer maleic anhydride grafted polyethylene-octene elastomer POE-g-MAH (maleic anhydride graft ratio 0.5%) and 0.7 wt% antioxidant β-(3,5-di-tert-butyl-4-hydroxyphenyl) stearyl propionate was stirred in a high-speed mixer for 5 minutes, and after uniform mixing, it was put into a twin-screw extruder for extrusion and granulation. The length-diameter ratio of the twin-screw extrusion equipment is 35, the control feeding speed is 8rpm / min, the screw speed is 200rpm / min, and the temperature of each zone of the screw barrel is 200°C for the first stage, 245°C for the second stage, and 245°C for the third stage. ℃, the fourth section is 245℃, the fifth section is 245℃, the sixth section is 245℃, the seventh section is 245℃, the ei...
Embodiment 3
[0037] 60% by weight of polyphenylene ether resin (intrinsic viscosity is 0.45dL / g), 20% by weight of high impact polystyrene resin, 10% by weight of elastomer 100nm ultrafine powder SBS, 7% by weight of bromine epoxy resin flame retardant, 2.8% by weight of compatibilizer maleic anhydride grafted polyethylene-octene elastomer POE-g-MAH (with maleic anhydride grafting rate of 0.3%) and 0.2% by weight of Antioxidant tris(2,4-di-tert-butylphenyl) phosphite was stirred in a high-speed mixer for 3 minutes, and after mixing uniformly, it was put into a twin-screw extruder for extrusion and granulation. The length-diameter ratio of the twin-screw extrusion equipment is 32, the control feeding speed is 5rpm / min, the screw speed is 300rpm / min, and the temperature of each zone of the screw barrel is 220°C for the first stage, 240°C for the second stage, and 240°C for the third stage. ℃, the fourth section is 245℃, the fifth section is 245℃, the sixth section is 245℃, the seventh sectio...
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