Polylactic acid foamed sheet and preparation method thereof
A technology of polylactic acid foaming and polylactic acid, which is applied in the field of polylactic acid foam sheet and its preparation, can solve the problems of polylactic acid foam sheet foaming unevenness, complicated preparation process, and uncontrollable cost, and achieve good results Industrial use value, good cell structure, and the effect of cell diameter
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Embodiment 1
[0041] (1) Add 98.8 parts of dry polylactic acid pellets, 1.0 parts of nucleating agent diphenyl dihydrazide sebacic acid, and 0.2 parts of chain extender 1,4-butanediol to a twin-screw extruder. In the extruder (model TDS-75D), after melt mixing (screw temperature 170-195°C) in a twin-screw extruder (screw diameter 75mm; aspect ratio 52:1), water cooling, pelletizing and drying Finally, polylactic acid foamed modified resin is obtained.
[0042] (2) Put the obtained polylactic acid foamed modified resin into the hopper of the foaming extruder formed by the two-stage extrusion system connected in series, wherein, the screw diameter of the one-stage extrusion system is φ90mm, and the length-to-diameter ratio is 32 : 1; the diameter of the screw of the secondary extrusion system is φ120mm, and the aspect ratio is 34:1. After the primary extrusion system is melted and plasticized, the blowing agent CCl is injected 3 F, the flow rate is 23.5kg / h, and the low-temperature homogeneo...
Embodiment 2
[0046] (1) Add 98.8 parts of dry polylactic acid pellets, 1.0 parts of nucleating agent diphenyl dihydrazide sebacic acid, and 0.2 parts of chain extender 1,4-butanediol to a twin-screw extruder. In the extruder (model TDS-75D), after melting and mixing (screw temperature: 170-195°C) in a twin-screw extruder (screw diameter: 75mm; aspect ratio: 52:1), water cooling, pelletizing, and drying , to obtain polylactic acid foamed modified resin.
[0047] (2) Put the obtained polylactic acid foamed modified resin into the hopper of the foaming extruder formed by the two-stage extrusion system connected in series, wherein, the screw diameter of the one-stage extrusion system is φ90mm, and the length-to-diameter ratio is 32 : 1; the diameter of the screw of the secondary extrusion system is φ120mm, and the aspect ratio is 34:1. After the primary extrusion system is melted and plasticized, the blowing agent CCl is injected 3 F, the flow rate is 28.5kg / h, and the low-temperature homogen...
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