Fusion graft process for modified polypropylene/acrylic acid polyester ether
A technology of polyether acrylate and melt grafting, which is applied in the field of polymer polymerization and processing, can solve the problems of continuous and uniform feeding, unstable grafting effect, etc., achieve quality improvement, avoid early decomposition, and ensure process stability Effect
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Embodiment 1
[0021] The preparation process is as follows: 100 parts of polypropylene, 5.0 parts of acrylic acid polyether monoester, 5.0 parts of diacrylic acid polyether diester, 0.1 part of initiator 2,5-dimethyl-2,5 di-tert-butylperoxyhexane (TX101), 0.3 parts of antioxidant (1010) were added to the high-speed disperser and mixed evenly, then added to the hopper of the twin-screw extruder, and carried out the grafting reaction of melt extrusion by co-rotating twin-screw extruder (screw diameter 35) . The temperature of each section of the twin-screw extruder is:
[0022] Zone I Zone II Zone III Zone IV Zone V Zone VI Zone VII Zone VIII Zone
[0023] 100°C 180°C 180°C 185°C 190°C 220°C 220°C 220°C 220°C
[0024] The screw speed is 45r / min, and the residence time of the material in the twin-screw is 3min. The extrudate is cooled and pelletized to obtain the grafted product.
Embodiment 2
[0026] 1) At room temperature, uniformly mix acrylic acid polyether monoester and diacrylic acid polyether diester in a high-speed mixer at a weight ratio of 1:1, and then add the initiator 2,5-dimethyl-2,5 bis-tertiary Butylperoxyhexane (TX101) and antioxidant tetrakis [β-(3,5-di-tert-butyl-4-hydroxyphenyl) propionate] pentaerythritol ester 1010, so that TX101 and antioxidant 1010 are mixed The weight concentration in the body is 1% and 3%.
[0027] 2), heat up the co-rotating twin-screw extruder (screw diameter 35), the temperature of each zone is as follows:
[0028] Zone I Zone II Zone III Zone IV Zone V Zone VI Zone VII Zone VIII Zone
[0029] 100°C 180°C 180°C 185°C 190°C 220°C 220°C 220°C 220°C
[0030] 3) Add polypropylene pellets to the twin-screw extruder through the feeding port for melt extrusion, and the feeding speed is controlled to be 10Kg / hour; at the same time, the mixed monomer solution is fed from the twin-screw extruder through a high-pressure metering p...
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