Reinforced and toughened polyadipic acid/butylene terephthalate-polylactic acid composite film and preparation method thereof
A technology of butylene terephthalate and polyadipic acid, used in sustainable manufacturing/processing, biological packaging, landfill technology, etc. Field, groundwater resource pollution and other issues, to achieve the effects of improved mechanical properties, good processing performance, and stable product performance
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Embodiment 1
[0026] Stir the dried 850g polyadipate / butylene terephthalate pellets, 150g polylactic acid pellets, and 1g cage-type silsesquioxane containing eight epoxy groups into the twin-screw extruder In the process, the temperature from zone 1 to the head is 170°C, 180°C, 190°C, 190°C, 190°C, 190°C, 180°C, the speed of the twin-screw extruder is 60r / min, and the material is extruded through the head After cooling, it is led to the high-speed granulator by the traction device for granulation. The pellets are dried again and poured into the film blowing machine for film blowing. By adjusting the screw speed, temperature, traction rate, crimping rate and blasting rate, etc., the film of the required specification can be blown. After the film is cooled, it can be packaged and stored. The longitudinal tensile strength of the obtained film is 29.71MPa, and the transverse direction is 19.82MPa. The elongation at break was 551% and 690% in the longitudinal and transverse directions, respect...
Embodiment 2
[0028] After the dried 850g polyadipate / butylene terephthalate pellets, 150g polylactic acid pellets, and 5g cage-type silsesquioxane containing eight epoxy groups are stirred, they are added to the twin-screw extruder In the process, the temperature from zone 1 to the head is 170°C, 180°C, 190°C, 190°C, 190°C, 190°C, 180°C, the speed of the twin-screw extruder is 60r / min, and the material is extruded through the head After cooling, it is led to the high-speed granulator by the traction device for granulation. The pellets are dried again and poured into the film blowing machine for film blowing. By adjusting the screw speed, temperature, traction rate, crimping rate and blasting rate, etc., the film of the required specification can be blown. After the film is cooled, it can be packaged and stored. The longitudinal tensile strength of the obtained film is 30.06MPa, and the transverse direction is 19.40MPa. The elongation at break was 555% and 647% in the longitudinal and tra...
Embodiment 3
[0030]Stir the dried 850g polyadipate / butylene terephthalate pellets, 150g polylactic acid pellets, and 10g cage-type silsesquioxane containing eight epoxy groups into the twin-screw extruder In the process, the temperature from zone 1 to the head is 170°C, 180°C, 190°C, 190°C, 190°C, 190°C, 180°C, the speed of the twin-screw extruder is 60r / min, and the material is extruded through the head After cooling, it is led to the high-speed granulator by the traction device for granulation. The pellets are dried again and poured into the film blowing machine for film blowing. By adjusting the screw speed, temperature, traction rate, crimping rate and blasting rate, etc., the film of the required specification can be blown. After the film is cooled, it can be packaged and stored. The longitudinal tensile strength of the obtained film is 29.34MPa, and the transverse direction is 19.46MPa. The elongation at break was 564% and 667% in the longitudinal and transverse directions, respect...
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