Halogen free antiflaming polycarbonate and rubber modified graft copolymer alloy and preparation method thereof
A technology of flame-retardant polycarbonate and graft copolymer, which is applied in the field of halogen-free flame-retardant polycarbonate and rubber-modified graft copolymer alloy and its preparation, can solve the problem of reducing the mechanical and thermal properties of PC alloys, reducing The impact strength of materials, reducing the thermal mechanical properties of materials, etc., to achieve the effects of reduced dosage, high flame retardancy and high heat resistance, and environmental friendliness
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Embodiment 1
[0062] Weigh the resin raw material and PTFE respectively according to the ratio shown in Table 2-2, and pre-mix them evenly with a high-speed mixing device at room temperature. After mixing evenly, add them to the extruder from the main hopper. After weighing and stirring evenly, use a special liquid feeding device to quantitatively add it to a TEX30a co-rotating twin-screw extruder (made by Japan Steel) for melt extrusion. The extrusion temperature is 230 ° C. Others are the same as Comparative Example 1. The results are shown in Table 2-1.
Embodiment 2
[0064] Weigh the resin raw materials, PX200 and TFE according to the proportions shown in Table 2-1, and pre-mix them evenly with a high-speed mixing and stirring device at room temperature. After mixing evenly, add them to the extruder from the main hopper. The liquid flame retardants RDP and BDP Also weighed in proportion and stirred evenly, quantitatively added to a TEX30a co-rotating twin-screw extruder (made by Japanese steel) with a special liquid feeding device for melt extrusion, the extrusion temperature was 230 ° C, and the others were the same as in Example 1 . The results are shown in Table 2-1.
Embodiment 3
[0066] Weigh the resin raw materials, TPP and PTFE according to the proportions shown in Table 2-1, and pre-mix them evenly with a high-speed mixing and stirring device at room temperature. After mixing evenly, add them to the extruder from the main hopper. BDP is also weighed in proportion and stirred evenly, and then quantitatively added to the TEX30a co-rotating twin-screw extruder (made by Japanese steel) with a special liquid feeding device for melt extrusion. The extrusion temperature is 230 ° C, and the others are the same as in Example 1. . The results are shown in Table 2-1.
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