Engineering plastic composition and preparation method thereof
A technology for engineering plastics and compositions, applied in the field of engineering plastic compositions and their preparation, can solve the problems of intolerant hydrolysis and difficult application, and achieve the effects of improving hydrolysis resistance, toughening effect and excellent hydrolysis resistance.
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Embodiment 1
[0033] 80 parts of PBT, 20 parts of ethylene-vinyl acetate-glycidyl methacrylate terpolymer and 0.3 parts of tetrakis[β-(3,5-di-tert-butyl-4-hydroxyphenyl) propionate] One part is pre-mixed evenly at room temperature, and then the premix is fed into the conveying section of the twin-screw extruder from the main feeding port, and one part of chain extender ADR4370 is added to the middle of the intermeshing section of the twin-screw extruder through side feeding, after continuous An engineering plastic composition can be obtained by melt extrusion (extrusion temperature is 240° C., screw rotation speed is 150 rpm).
Embodiment 2
[0035] 80 parts of PET, 20 parts of ethylene-vinyl acetate-glycidyl methacrylate terpolymer, 0.2 parts of tris[2,4-di-tert-butylphenyl]phosphite and β-(3,5- 0.2 parts of n-octadecyl di-tert-butyl-4-hydroxyphenyl) propionate are premixed evenly at room temperature, and then the premix is fed into the conveying section of the twin-screw extruder from the main feed port, and fed through the side Add 0.8 parts of chain extender ADR4468 to the middle part of the intermeshing section of the twin-screw extruder, and obtain an engineering plastic composition through continuous melt extrusion (extrusion temperature is 255° C., screw speed is 180 rpm).
Embodiment 3
[0037] 75 parts of PBT, 10 parts of ethylene-vinyl acetate-glycidyl methacrylate terpolymer, 15 parts of ethylene-vinyl acetate binary copolymer, tetrakis[β-(3,5-di-tert-butyl- 0.15 parts of 4-hydroxyphenyl) propionic acid] pentaerythritol ester, 0.15 parts of tris [2,4-di-tert-butylphenyl] phosphite and 0.1 part of solid paraffin were premixed at room temperature, and then the premix was prepared by The main feeding port is added to the conveying section of the twin-screw extruder, and 1.2 parts of chain extender hexamethylene diisocyanate is added to the middle of the intermeshing section of the twin-screw extruder through side feeding, and is continuously melted and extruded (extrusion temperature is 235 °C, the screw speed is 210rpm) to obtain an engineering plastics composition.
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