Ultrahigh molecular weight polyethylene composition capable of being extrusion molded and its prepn process
An ultra-high molecular weight, extrusion molding technology, applied in the field of ultra-high molecular weight polyethylene composition and its preparation, can solve the problems of application and promotion limitations, many processing aids, poor adaptability, etc. Low, the effect of maintaining mechanical properties
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Embodiment 1
[0035] Example 1: Add 100g of polyethylene glycol with a molecular weight of 2000 and 50g of montmorillonite with an average particle size of 100nm into a high-speed mixer, seal it, stir at a high speed of 70°C for 10 minutes, and discharge after cooling to obtain composite processing Auxiliary MP I, then 90g of ultra-high molecular weight polyethylene with a molecular weight of 2.50±500,000 and 10g of polypropylene (F401) with MI=2.3g / min, 3g of compound processing aid MP I, 0.5g of sodium benzoate, 2, 0.3 g of 6-di-tert-butyl-4-ethylphenol and 0.3 g of glycerol trihydroxystearate were uniformly mixed, and granulated by twin-screw extrusion. The extrusion temperature of each section from the feed inlet to the discharge outlet is: 170-200°C, 190°C-220°C, 200°C-220°C, 180°C-220°C. The properties of the obtained pellets are shown in Table 1.
Embodiment 2
[0036] Embodiment 2: the molecular weight is 350 ± 500,000 ultra-high molecular weight polyethylene 80g and the polypropylene (F401) 20g of MI=2.3g / min, composite processing aid MP I 4g, talcum powder 0.2g, 4-methylol 0.2 g of base-2,6-di-tert-butylphenol and 0.2 g of oxidized polyethylene wax were uniformly mixed, and pelletized by twin-screw extrusion. All the other components and operating conditions are with embodiment 1 in the prescription. The results are shown in Table 1.
Embodiment 3
[0037] Embodiment 3: the molecular weight is 450 ± 500,000 ultra-high molecular weight polyethylene 70g and polypropylene (F401) 30g of MI=2.3g / min, composite processing aid MP I 5g, mica 1.0g, phosphorous acid tris(2 , 1.0 g of 4-di-tert-butylphenyl) ester and 1.0 g of stearic acid amide were uniformly mixed, and granulated by twin-screw extrusion. All the other components and operating conditions are with embodiment 1 in the prescription. The results are shown in Table 1.
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