Method for preparing compatilizer system by using polyphenyl ether as base material
A technology of polyphenylene ether and compatibilizer, which is applied in the field of preparation of compatibilizer system, can solve the problems of poor fluidity, easy cracking and large internal stress of products in PPO processing, and achieve the effect of perfect continuous production operation
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Embodiment 1
[0047] (the flow chart adds MAH earlier, and then accelerator, and it is like this in the embodiment)
[0048] (1) Preparation of grafted transparent mixture
[0049] Weigh 4 parts of maleic anhydride (MAH) and methyl ethyl ketone in proportion, stir and dissolve, add 1 part of caprolactam (CALA), stir and dissolve, then add 0.20 parts of accelerator (DTBH), and stir to form a transparent mixed solution;
[0050] Weigh 4 parts of maleic anhydride (MAH) and methyl ethyl ketone in proportion, stir and dissolve, then add 0.20 parts of accelerator (DTBH), and stir to form a transparent mixed solution;
[0051] (2) 100 parts of PPO after drying at 95-100°C for 3-4 hours, add to the mixer to mix and disperse;
[0052] (3) Gradually (spray) the transparent mixture into the mixer, and control it to mix evenly at 60°C;
[0053] (4) Add the mixed material into the feed hopper of the reaction extrusion pelletizer material, input the extruder through the metering screw, and carry out th...
Embodiment 2
[0066] (1) Preparation of grafted transparent mixture
[0067] Weigh 4 parts of maleic anhydride (MAH) and methyl ethyl ketone in proportion, stir and dissolve, then add 0.20 parts of accelerator (DTBH), and stir to form a transparent mixed solution;
[0068] (2) 100 parts of PPO after drying at 90-100°C for 3-4 hours, add to the mixer to mix and disperse;
[0069] (3) Gradually (spray) the transparent mixture into the mixer, and control it to mix evenly at 60°C;
[0070] (4) Add the mixed material into the feed hopper of the reaction extrusion pelletizer material, input the extruder through the metering screw, and carry out the blending reaction extrusion pelletization at 170-260°C to obtain the corresponding PPO Compatibilizer system: PPO-g-MAH.
[0071] The extrusion temperature of the extruder is 170-180°C in zone 1, 180-190°C in zone 2, 195-205°C in zone 3, 215-235°C in zone 4, 245-255°C in zone 5, 255-260°C in zone 6, and 255-260°C in zone 7. 250-260°C, die head 250-2...
Embodiment 3
[0082] (1) Preparation of grafted transparent mixture
[0083] Weigh 4 parts of maleic anhydride (MAH) and methyl ethyl ketone in proportion, stir and dissolve, then add 0.20 parts of accelerator (DTBH), and stir to form a transparent mixed solution;
[0084] (2) Add 50 parts of PPO and 50 parts of SEBS after drying at 90-100°C for 3-4 hours into the mixer for mixing and dispersing;
[0085] (3) Gradually (spray) the transparent mixture into the mixer, and control it to mix evenly at 60°C;
[0086] (4) Add the mixed material into the feed hopper of the reaction extrusion pelletizer material, input the extruder through the metering screw, and carry out the blending reaction extrusion pelletization at 170-260°C to obtain the corresponding PPO Compatibilizer system: PPO-g-MAH.
[0087] The extrusion temperature of the extruder is 170-180°C in zone 1, 180-190°C in zone 2, 195-205°C in zone 3, 215-235°C in zone 4, 245-255°C in zone 5, 255-260°C in zone 6, and 255-260°C in zone 7....
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