High-rigidity high-impact polypropylene resin composition and preparation method thereof
A high-impact polypropylene and polypropylene resin technology, applied in the field of polypropylene materials, can solve the problems of not meeting the requirements of buried polypropylene pipes for ring stiffness and low rigidity of polypropylene resins.
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Embodiment 1
[0028] A high-rigidity high-impact polypropylene resin composition, according to parts by weight, its formula is:
[0029]
[0030]
[0031] Preparation method: Mix the above-mentioned polypropylene resin, antioxidant, halogen absorbent, polymer processing aid, α-nucleating agent, and β-nucleating agent in a high-speed mixer for 5 minutes, and then add the uniformly mixed materials to the double It is produced by melting, plasticizing, extruding and granulating in a screw extruder. Wherein, the aspect ratio of the screw of the twin-screw extruder is 30, and the diameter of the screw of the twin-screw extruder is 25mm. The processing temperature range of the twin-screw extruder is 200-230°C. The properties of the obtained polypropylene resin are shown in Table 2.
Embodiment 2
[0033] A high-rigidity high-impact polypropylene resin composition, according to parts by weight, its formula is:
[0034]
[0035] Preparation method: mix polypropylene resin, antioxidant, halogen absorbent, polymer processing aid, α-nucleating agent, and β-nucleating agent in a high-speed mixer for 4 minutes, and then add the uniformly mixed materials to It is produced by melting, plasticizing, extruding and granulating in a twin-screw extruder. Wherein, the aspect ratio of the screw of the twin-screw extruder is 30, and the diameter of the screw of the twin-screw extruder is 72 mm. The processing temperature range of the twin-screw extruder is 200-230°C. The properties of the obtained polypropylene resin are shown in Table 2.
Embodiment 3
[0037] A high-rigidity high-impact polypropylene resin composition, according to parts by weight, its formula is:
[0038]
[0039] Preparation method: Mix the above-mentioned polypropylene resin, antioxidant, halogen absorbent, polymer processing aid, α-nucleating agent, and β-nucleating agent in a high-speed mixer for 5 minutes, and then add the uniformly mixed materials to the double It is produced by melting, plasticizing, extruding and granulating in a screw extruder. Wherein, the aspect ratio of the screw of the twin-screw extruder is 30, and the diameter of the screw of the twin-screw extruder is 35mm. The processing temperature range of the twin-screw extruder is 190-220°C. The properties of the obtained polypropylene resin are shown in Table 2.
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