Method for improving metallocene polyethylene cross-linking efficiency and optimizing net structure of conjugate
A technology for metallocene polyethylene and cross-linking efficiency, which is applied in the fields of improving the cross-linking efficiency of metallocene polyethylene and optimizing the network structure of cross-linked products, and can solve the problems that it is difficult to play a long-term anti-aging effect and affect the initiation efficiency of initiators. , to achieve the effect of improving initiation efficiency, improving mechanical properties, and eliminating acidic impurities
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Embodiment 1
[0035] (1) premixing: 991g melt flow rate is the metallocene polyethylene (produced by EXXON company, the trade mark is EXCEED 1018FA) of 1.0g / 10min, 1g phosphate nucleating agent (produced by GREAT LAKE company, the trade mark is CLEARLITE NU011), 5g of white carbon black (manufactured by DEGUSSA company, brand A200), 3g of DTBP initiator, according to the sequence of metallocene polyethylene, phosphate nucleating agent, white carbon black and DTBP initiator, add the speed at 80-100 rpm A low-speed mixer, pre-mixed at 20-30°C for 2-3 minutes to form a mixture;
[0036] (2) Cross-linking: Add the material mixed in step (1) into the co-rotating parallel twin-screw extruder, control the extrusion temperature of each section to 160-180°C, and the screw speed to 150-250 rpm. The rotation speed of the machine is 20-50 rpm to obtain a metallocene polyethylene cross-linked product.
[0037] Its product properties are shown in Table 1.
example 2
[0039] (1) Premixing: 990g of metallocene polyethylene with a melt flow rate of 1.0g / 10min, 2g of phosphate nucleating agent, 5g of white carbon black, 3g of DTBP initiator, according to the metallocene polyethylene, phosphate nucleating agent , white carbon black and DTBP initiator are sequentially added to a low-speed mixer with a rotation speed of 50-100 rpm, and pre-mixed at 30-40°C for 1-5 minutes to form a mixture;
[0040] (2) Cross-linking: Add the material mixed in step (1) into the co-rotating parallel twin-screw extruder, control the extrusion temperature of each section to 150-180°C, and the screw speed to 100-200 rpm. The rotation speed of the machine is 10-40 rpm to obtain a metallocene polyethylene cross-linked product.
[0041] Its product properties are shown in Table 1, and its microscopic morphology is shown in Table 1. figure 1 .
example 3
[0043] (1) Premixing: 989g metallocene polyethylene with a melt flow rate of 1.0g / 10min, 3g phosphate nucleating agent, 5g white carbon black, 3g DTBP initiator, according to metallocene polyethylene, phosphate nucleating agent 1. Add carbon black and DTBP initiator sequentially to a low-speed mixer with a rotation speed of 100-200 rpm, and pre-mix for 5-10 minutes at 20-30°C to form a mixture;
[0044] (2) Cross-linking: Add the material mixed in step (1) into the co-rotating parallel twin-screw extruder, control the extrusion temperature of each section to 160-200°C, and the screw speed to 200-300 rpm. The rotation speed of the machine is 40-80 rpm to obtain a metallocene polyethylene cross-linked product.
[0045] Its product properties are shown in Table 1.
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