A kind of preparation method of polypropylene foam beads
A foaming bead and polypropylene technology, applied in the field of polymers, can solve the problems of high melting point, high molding temperature, increased energy consumption and manufacturing cost, etc.
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[0045] Preparation of matrix resin HMSPP501
[0046] The polymerization reaction was carried out on a polypropylene pilot plant. Its main equipment includes prepolymerization reactor, first loop reactor and second loop reactor.
[0047] Pre-polymerization reaction: the main catalyst (DQ-III catalyst, provided by Beijing Aoda Branch of Sinopec Catalyst Company) with a flow rate of about 0.5g / hr, the co-catalyst (triethylaluminum) with a flow rate of 6.33g / hr, and a flow rate of 0.63 g / hr of the first external electron donor (dicyclopentyldimethoxysilane, DCPMS) was pre-contacted at 6°C for 20 minutes, and then continuously added to the continuous stirred tank prepolymerization reactor for prepolymerization reaction. Prepolymerization It is carried out under the environment of the propylene liquid phase body, the temperature is 15°C, and the residence time is about 4 minutes. Under these conditions, the prepolymerization ratio of the catalyst is about 120 to 150 times. The TEA...
Embodiment 1~10
[0058] 1) Preparation of polypropylene resin particles: put 100 parts by weight of matrix resin, 0.05 parts by weight of cell nucleating agent (silicon dioxide) and additives into a high-speed mixer and mix at high speed for 30 seconds, then add LabLine100 microparticle preparation system , the torque is controlled at about 65%, the rotation speed is 300rpm, and the polypropylene resin particles are obtained by underwater pelletizing. Wherein, the matrix resin used in Examples 1-5 is HMSPP501, and the matrix resin used in Examples 6-10 is HMSPP502. The used additive of embodiment 1~10 all comprises the antioxidant 1010 (BASF company) of 0.2 weight part, the antioxidant 168 (BASF company) of 0.1 weight part and the calcium stearate of 0.05 weight part. Specifically, after blending the matrix resin, cell nucleating agent and additives with a high-speed mixer, extruding through a twin-screw extruder, introducing a temperature of 75°C or below, preferably 70°C or below, more prefe...
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