Compatibilizer and thermoplastic resin employing the same
A technology of thermoplastic resin and compatibilizer, which is applied in the field of thermoplastic resin composition, and can solve problems affecting mechanical properties, etc.
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preparation example 1
[0023] Get 1.98 kilograms of polypropylene fat pellets (PP) and directly feed to the twin-screw extruder, then take 0.02 kilograms of acrylic acid (acrylic acid, AA) and 2 g of 2,5-dimethyl-2,5-bis(tert Butylperoxy)hexane (as a peroxide free radical initiator) was fed to the aforementioned twin-screw extruder in a side-feed manner. The temperature of the screw feed port is 200°C, the temperature of the injection section is 210°C, the screw speed is 200rpm, and the mixing time is about 1 minute. Finally, the finished product is cooled and granulated with water to obtain polypropylene (PP- AA) color masterbatch, the weight percent of reactive groups is about 1wt%.
preparation example 2
[0025] Get 1.98 kg of polypropylene pellets (PP) directly into the twin-screw extruder, then take 0.02 kg of maleic anhydride (maleic anhydride, MAH) and 2 g of 2,5-dimethyl-2,5 - Di(tert-butylperoxy)hexane (as peroxide radical initiator) was fed as side feed to the aforementioned twin-screw extruder. The temperature of the screw feed port is 200°C, the temperature of the injection section is 210°C butene, the screw speed is 200rpm, and the mixing time is about 1 minute. Finally, the finished product is cooled and granulated with water to obtain a maleic anhydride derivative group. Polypropylene (PP-MAH) liposomes, the weight percent of reactive groups is about 1wt%.
[0026] Preparation of Ethylene-Propylene-Conjugated Diene Copolymers with Reactive Groups
preparation example 3
[0028] Get 1.98 kilograms of EPDM rubber (EPDM, product number KEP2320, sold by KUMHO) directly into the twin-screw extruder, then get 0.02 kilograms of maleic anhydride (maleicanhydride, MAH) and 2g of 2,5 - Dimethyl-2,5-bis(tert-butylperoxy)hexane (as peroxide free radical initiator) was fed as side feed to the previously described twin-screw extruder. The temperature of the screw feed port is 200°C, the temperature of the injection section is 210°C, the screw speed is 200rpm, and the mixing time is about 1 minute. Finally, the finished product is cooled and granulated with water to obtain three For ethylene-propylene-diene rubber (EPDM-MAH) liposomes, the weight percent of reactive groups is about 1wt%.
[0029] Copolymer preparation with formula (I) structure
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