Extrusion foaming polypropylene particles with lower thermal molding pressure 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
[0045] 4 kilograms of β-nucleating agent masterbatch, 66.4 kilograms of high melt strength polypropylene (RS1684, Basell Company), 30 kilograms of linear isotactic polypropylene (F401, Liaoning Huajin Company), 0.1 kilogram of antioxidant 168, 0.2 kilogram Antioxidant 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, and the supercritical carbon dioxide The injection speed was controlled at 3 kg per hour, the head pressure was 17 MPa, the head temperature was 160°C, and the water temperature of the underwater pelletizer was controlled at 60°C to obtain expanded polypropylene beads with an expansion ratio of 30 times.
[0046] The obtained foamed polypropylene beads are put into a thermoforming machine for molding, the steam pressure is 0.4 MPa (welding temperature is 144° C.), the ...
Embodiment 2
[0048] 6 kilograms of β-nucleating agent masterbatch, 44.6 kilograms of high melt strength polypropylene (RS1684, Basell Company), 50 kilograms of linear isotactic polypropylene (F401, Liaoning Huajin Company), 0.1 kilogram of antioxidant 168, 0.2 kilogram Antioxidant 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, and the supercritical carbon dioxide The injection speed was controlled at 2.8 kg per hour, the head pressure was 14MPa, the head temperature was 170°C, and the water temperature of the underwater pelletizer was controlled at 40°C to obtain expanded polypropylene beads with an expansion ratio of 23 times.
[0049] The obtained foamed polypropylene beads are put into a thermoforming machine for molding, the steam pressure is 0.45 MPa (welding temperature is 148° C.), th...
Embodiment 3
[0051] 4 kilograms of β-nucleating agent masterbatch, 66.4 kilograms of high melt strength polypropylene (RS1684, Basell Company), 30 kilograms of linear isotactic polypropylene (F401, Liaoning Huajin Company), 0.1 kilogram of antioxidant 168, 0.2 kilogram Antioxidant 1010, 1 kg of calcium stearate, after mixing evenly, put it into the extruder to extrude and foam. The materials can be added continuously according to the ratio of the above raw materials for continuous production. The extrusion speed of the materials is controlled at an hourly extrusion rate 40 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 with a foaming ratio of 24 times beads.
[0052] The obtained foamed polypropylene beads are put into a thermoforming machine for molding, the steam pressure is 0.45...
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