Preparation method of maleic anhydride grafted polypropylene
A technology of grafting polypropylene and maleic anhydride, which is applied in the field of preparation of maleic anhydride grafted polypropylene, can solve the problem of difficult to obtain high maleic anhydride grafting rate and mechanical properties of maleic anhydride grafted polypropylene and polypropylene Grafting rate decline and other issues, to achieve stable free radical concentration, free radical coupling termination rate decreased, and inhibit degradation effect
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Embodiment 1
[0034] 7.5Kg styrene and 0.4Kg initiator dicumyl peroxide (product of Shanghai Gaoqiao Petrochemical) were mixed and dissolved. Mix 100Kg of polypropylene (product of Shanghai Petrochemical Co., Ltd., brand: Y1600, melt index: 16g / min) and 5.0Kg of maleic anhydride in a high mixer. Then, the mixture of polypropylene and maleic anhydride is fed into a twin-screw extruder with a screw diameter of 57mm, a length-to-diameter ratio of 60:1, and a total of 15 screw barrel sections at a speed of 1.2Kg / min. The initiator / styrene solution is input through the metering pump through two feeding ports. The first feeding port is in the 4th screw barrel section, the second feeding port is in the 7th screw barrel section, and the speed of each feeding port is 45g / min respectively. The barrel temperature was set at 180° C., and the rotation speed of the extruder was 90 rpm. In the 13th barrel section, the liquid antioxidant 2,6-di-tert-butyl-4-n-butylphenol is input at a speed of 5 g / min. ...
Embodiment 2
[0044] 7.5Kg styrene and 0.4Kg initiator dicumyl peroxide (product of Shanghai Gaoqiao Petrochemical) were mixed and dissolved. Mix 100Kg of polypropylene (product of Shanghai Petrochemical Co., Ltd., brand: Y1600, melt index: 16g / min) and 5.0Kg of maleic anhydride in a high mixer. Then, the mixture of polypropylene and maleic anhydride was fed into a two-stage twin-screw extruder at a rate of 1.2 Kg / min. The screw diameter of the first-stage twin-screw extruder is 57mm, the aspect ratio is 60:1, and a total of 15 screw barrel segments; the screw diameter of the second-stage twin-screw extruder is 65mm, the aspect ratio is 28:1, a total of 7 screw barrel segment. The initiator / styrene solution is input through the metering pump through three feeding ports. The first feeding port is in the 4th screw barrel section of the first-stage twin-screw extruder, the second feeding port is in the 8th screw barrel section of the first-stage twin-screw extruder, and the third feeding por...
Embodiment 3
[0054] 3.0Kg styrene and 0.4Kg initiator dicumyl peroxide (product of Shanghai Gaoqiao Petrochemical) were mixed and dissolved. Mix 100Kg of polypropylene (product of Shanghai Petrochemical Co., Ltd., brand: Y1600, melt index: 16g / min) and 5.0Kg of maleic anhydride in a high mixer. Then, the mixture of polypropylene and maleic anhydride is fed into a twin-screw extruder with a screw diameter of 57mm, a length-to-diameter ratio of 60:1, and a total of 15 screw barrel sections at a speed of 1.2Kg / min. The initiator / styrene solution is input through the metering pump through two feeding ports. The first feeding port is in the 4th screw barrel section, the second feeding port is in the 7th screw barrel section, and the speed of each feeding port is 19.5g / min respectively. The barrel temperature was set at 180° C., and the rotation speed of the extruder was 90 rpm. In the 13th barrel section, the liquid antioxidant 2,6-di-tert-butyl-4-n-butylphenol is input at a speed of 5 g / min....
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