Composite slipping and anti-blocking masterbatch with high surface tension for BOPP (Biaxially Oriented Polypropylene) film and production process of masterbatch
An anti-blocking masterbatch and production process technology, applied in the field of functional additives for plastic films, can solve the problems of unsustainable film smoothness, high surface friction coefficient, burden, etc., so as to avoid the problem of pre-dispersion and reduce the friction coefficient. , the effect of reducing film resistance
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Embodiment 1
[0030] The weight percentage composition of the slip and anti-blocking masterbatch is as follows:
[0031]
[0032] The high-efficiency slip agent is a mixture of silicone, silicone powder and polypropylene wax in a weight ratio of 2:2:1; the highly dispersible anti-blocking agent is silica particles with an average particle size of 3μm and an average particle size of 5μm. A mixture of silicone resin particles and plexiglass beads with an average particle size of 5μm in a weight ratio of 2:3:5.
[0033] The production process of the slip and anti-blocking masterbatch of Example 1 is as follows: Weigh the raw materials of each component, mix the weighed raw materials through a mixer at a speed of 80r / min, and then pass the mixed raw materials through a twin-screw extruder Melt extrusion, then dry, cool, pelletize and shape;
[0034] The production temperature of each zone of the twin-screw extruder is shown in Table 2. The melt pressure of the twin-screw extruder is 2.5Mpa, the host ...
Embodiment 2
[0038] The weight percentage composition of the slip and anti-blocking masterbatch is as follows:
[0039]
[0040] The high-efficiency slip agent is a mixture of polyethylene wax and silicone powder; the high-dispersion anti-blocking agent is a mixture of silica particles and diatomaceous earth.
[0041] The production process of Example 2 is as follows: Weigh the raw materials of each component, mix the weighed raw materials uniformly through a mixer at a speed of 80r / min, and then melt and extrude the mixed raw materials through a twin-screw extruder, and then Drying, cooling, pelletizing and forming;
[0042] The range of production temperature in each zone of the twin-screw extruder is controlled the same as in the first embodiment. The melt pressure of the twin-screw extruder is 2.45Mpa, the current of the main machine is controlled at 43A, the main machine speed is controlled at 300r / min, and the feeding speed is controlled. At 29r / min, the pelletizer speed is 385r / min.
Embodiment 3
[0044] The weight percentage composition of the slip and anti-blocking masterbatch is as follows:
[0045]
[0046] The polypropylene copolymer is a mixture of ethylene-propylene copolymer and ethylene-propylene-octene copolymer. The high-efficiency slip agent is silicone powder, the high-dispersion anti-blocking agent is silicone resin, and the polymer graft is A mixture of polypropylene grafted maleic anhydride, EPDM grafted maleic anhydride, and POE grafted maleic anhydride.
[0047] The production process of Example 3 is as follows: Weigh the raw materials of each component, mix the weighed raw materials uniformly through a mixer at a speed of 80r / min, and then melt and extrude the mixed raw materials through a twin-screw extruder. Drying, cooling, pelletizing and forming;
[0048] The production temperature range of each zone of the twin-screw extruder is controlled in Table 3. The melt pressure of the twin-screw extruder is 2.5Mpa, the current of the main machine is controlled...
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