Extrusion foaming polypropylene particles with lower thermal molding temperature and preparation method thereof
A technology for extruding foam and polypropylene, applied in the field of polymer foam material production, can solve the problems of inapplicability, complex production process, and impact on the service life of products, and achieve high mechanical strength and thermal deformation temperature, high production The effect of efficiency
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Embodiment 1
[0047] 4 kg of β-nucleating agent masterbatch, 66.4 kg of high melt strength polypropylene (RS1684, Basell Company), 30 kg of block copolymer polypropylene (K8303, Yanshan Petrochemical Company), 0.1 kg of antioxidant 168, 0.2 kg of anti-oxidant Oxygen agent 1010, after mixing evenly, put it into the extruder to extrude and foam. The material can be continuously added according to the above raw material ratio for continuous production. The extrusion speed of the material is controlled at 40 kg per hour. The injection of supercritical carbon dioxide The speed is controlled to inject 3 kg per hour, the head pressure is 17MPa, the head temperature is 160°C, and the water temperature of the underwater pelletizer is controlled at 60°C to obtain expanded polypropylene beads with an expansion ratio of 30 times. The DSC curve of the expanded polypropylene beads is shown in figure 1 .
[0048] The obtained expanded polypropylene beads are put into a thermoforming machine for molding, ...
Embodiment 2
[0050] 6 kg of β-nucleating agent master batch, 44.6 kg of high melt strength polypropylene (RS1684, Basell Company), 50 kg of block copolymer polypropylene (K8303, Yanshan Petrochemical Company), 0.1 kg of antioxidant 168, 0.2 kg of anti-oxidant Oxygen agent 1010, after mixing evenly, put it into the extruder to extrude and foam. The material can be continuously added according to the above raw material ratio for continuous production. The extrusion speed of the material is controlled at 40 kg per hour. The injection of supercritical carbon dioxide The speed is controlled to inject 2.8 kg per hour, the head pressure is 14MPa, the head temperature is 170°C, and the water temperature of the underwater pelletizer is controlled at 40°C to obtain expanded polypropylene beads with an expansion ratio of 24 times.
[0051] The obtained foamed polypropylene beads are put into a thermoforming machine for molding, the steam pressure is 0.47 MPa (welding temperature is 150° C.), the surfa...
Embodiment 3
[0053] 4 kg of β-nucleating agent masterbatch, 66.4 kg of high melt strength polypropylene (RS1684, Basell Company), 30 kg of block copolymer polypropylene (K8303, Yanshan Petrochemical Company), 0.1 kg of antioxidant 168, 0.2 kg of anti-oxidant Oxygen agent 1010, 1 kilogram of calcium stearate, put into the extruder after mixing evenly and extrude foaming, can add material continuously according to the above-mentioned raw material ratio, carry out continuous production, and the extrusion speed of material is controlled at extruding 40 per hour kg, the injection speed of supercritical carbon dioxide is controlled at 2.8 kg per hour, the head pressure is 15MPa, the head temperature is 150°C, and the water temperature of the underwater pelletizer is controlled at 60°C to obtain expanded polypropylene beads with an expansion ratio of 23 times grain.
[0054] The obtained foamed polypropylene beads are put into a thermoforming machine for molding, the steam pressure is 0.45 MPa (w...
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