Electret high-melt-index polypropylene master batch and preparation method thereof
A polypropylene, high-body technology, applied in the field of electret high-melting index polypropylene masterbatch and its preparation, can solve the problems of increasing the electrostatic adsorption and negative ion sterilization ability of melt-blown cloth, the material is difficult to disperse, and the nozzle is easy to block, and achieves Avoid the problem of nozzle clogging, improve the filtering effect and reduce the resistance effect
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[0039] Another embodiment of the present application provides a method for preparing an electret high melting point polypropylene masterbatch, the steps comprising:
[0040] 101. Mixing the raw materials;
[0041] Mix polypropylene powder and di-tert-butyl peroxide evenly in a low-speed mixer;
[0042] Put in nucleating agent, antioxidant, lubricant and dielectric, mix and disperse evenly in a low-speed mixer.
[0043] 102. Feed the mixed material into the extruder;
[0044] The extruder is a twin-screw extruder, the length-to-diameter ratio of the twin-screw extruder is 48-60, the temperature of the extruder barrel is set at 160-265°C; the screw speed is 300-600 rpm, and the feeder speed is 28-48HZ, polypropylene undergoes free radical degradation reaction under the action of organic peroxide initiator, high temperature melting and screw shearing, and complete degradation will not block the spinneret.
[0045] 103. Carry out vacuum devolatilization treatment on the materia...
Embodiment 1
[0053] Example 1: 50kg of polypropylene powder (grade 230 powder) and 600ml of di-tert-butyl peroxide were mixed evenly in a low-speed mixer, and 150 grams of compounded transparent nucleating agent, 200 g of antioxidant 1010, and 150 g of lubricant FFB were added , 75g dielectric, 50kg polypropylene powder (grade 230 powder) are mixed evenly and dispersed in the low-speed mixer of the mixer, and the mixed material is fed to the extruder through the hopper of the intermediate feeding system;
[0054] The aspect ratio of the twin-screw extruder is 48-60; the barrel temperature of the extruder is set at 160-250°C; the screw speed is 300-600 rpm, and the feeder speed is 28--48 Hz; polypropylene Under the action of organic peroxide initiator, high temperature melting and screw shearing, free radical degradation reaction occurs, complete degradation will not block the spinneret.
[0055] Vacuum devolatilization controls the vacuum degree at -0.12~-0.08MPa, exhausts devolatilization...
Embodiment 2
[0061] Example 2: 50kg of polypropylene powder (grade 230 powder) and 700ml of di-tert-butyl peroxide are mixed evenly in a low-speed mixer, and 200 grams of compound transparent nucleating agent, 250g of 1010 antioxidant, and 200g of lubricant FFB are added Mix and 100g dielectric in the low-speed mixer of the mixer and disperse evenly, and the mixed material is fed to the extruder through the hopper of the intermediate feeding system;
[0062] The aspect ratio of the twin-screw extruder is 48-60; the barrel temperature of the extruder is set at 160-250°C; the screw speed is 300-600 rpm, and the feeder speed is 28--48 Hz; polypropylene Under the action of organic peroxide initiator, high temperature melting and screw shearing, free radical degradation reaction occurs, the molecular weight changes from high to low, and the melt index changes from low to high;
[0063] Vacuum devolatilization controls the vacuum degree at -0.12~-0.08MPa, exhausts devolatilization and stabilizat...
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