Polyolefin masterbatch and preparation method thereof
A color masterbatch and polyolefin technology, applied in the field of plastic coloring, can solve the problems of easy to produce flow pattern, uneven color, large color difference, etc., and achieve the effect of overcoming flow pattern, not easy to sink, and excellent in dispersibility.
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Embodiment 1
[0016] Under normal temperature and pressure, mix the following components and weight percentages: LDPE 20%, LLDPE 30%, titanium dioxide 40%, polyethylene wax 8%, water 2%, and mix at high speed in a high-speed mixer for 10 minutes, using a twin screw The extruder is melted and blended, the temperature is controlled at 190°C, the screw speed is 200r / min, the pigment is uniformly dispersed in the carrier resin through the shearing and mixing of the screw, and then water-cooled stranding granulation is performed to obtain the columnar invention. Of masterbatch.
Embodiment 2
[0018] Under normal temperature and pressure, the following components and weight percentages: EVA 23%, LDPE 12%, lithopone 35%, phthalocyanine green 1%, ultramarine blue 2%, EBS 2%, oxidized polyethylene wax 8%, white Mineral oil 2%, phosphite 168 2%, azodicarbonamide (ADC) 1%, 4,4'-oxobis (sulfonyl semicarbazide) 2%, dicumyl peroxide (DCP) 1 %, di-tert-butyl peroxide (DTBP) 1%, calcium carbonate 8%. High-speed mixing is carried out in a high-speed mixer for 15 minutes, and after mixing to a temperature of 165° C. by banburying, air-cooling and hot-cutting granulation are used to prepare the disc-shaped masterbatch of the present invention.
Embodiment 3
[0020] Under normal temperature and pressure, the following components and weight percentages: LDPE 60%, POE 10%, iron oxide red 20%, polyethylene glycol 7%, OBSH 2%, antioxidant 1010 1%, in a high-speed mixer Perform high-speed mixing for 10 minutes in the medium, and use a twin-screw extruder for melt blending. The temperature is controlled at 180°C and the screw speed is 200r / min. Through the shearing and mixing of the screw, the pigment is evenly dispersed in the carrier resin. The color masterbatch of the present invention is obtained by water-cooled drawing and granulation.
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