A kind of thermoplastic micro-airbag polymer elastomer material and preparation method thereof
A technology of elastomer materials and polymer materials, which is applied in the field of thermoplastic micro-airbag polymer elastomer materials and its preparation, can solve problems such as instability and simple control methods, and achieve the effect of improving energy absorption and energy storage
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[0063] As a preferred embodiment, the preparation method of the thermoplastic microbag polymer elastomer material includes the following steps:
[0064] (1) Feed the supporting framework polymer material, the pressure-resistant slow-resilient polymer material and the nucleating agent from the front end of the twin-screw extruder, and the foaming agent from the mid-section feeding port of the twin-screw extruder to make After the raw materials are fully hot-melted and mixed, they enter the static mixer for further homogenization, and then are pressure-controlled and quantitatively transported by the melt pump;
[0065] (2) The hot melt pumped by the melt enters the underwater pelletizing chamber through the die to cut pellets, and is carried out and separated by the process water. The resulting pellets are screened and dried to form the target product.
[0066] As a more preferred embodiment of the above-mentioned preferred embodiment, the temperature of the twin-screw extruder in ste...
Embodiment 1
[0075] According to the above as figure 1 The process flow of preparing the thermoplastic micro airbag polymer elastomer material of the present invention according to the following raw material formula and process conditions:
[0076] Among them, the molecular weight M w In 150K~300K (here K means unit thousand) of polyether thermoplastic polyurethane, adding ratio 75% (weight percentage, the same below), molecular weight M w In the 50K~100K polyether thermoplastic polyurethane, the adding ratio is 20%, the blowing agent is CO 2 , The addition amount is 4.5%, the nucleating agent is calcium carbonate, and the addition amount is 0.5%. Twin-screw extruder L / D=40, screw heating temperature 160-220℃, static mixer temperature 140-180℃, melt pump inlet pressure 100-120bar, process water pressure about 12bar, controlled pressure release The difference (that is, the pressure difference between the high-pressure hot melt at the die outlet and the process water in the underwater cutting ch...
Embodiment 2
[0080] According to the above as figure 1 The process flow of preparing the thermoplastic micro airbag polymer elastomer material of the present invention according to the following raw material formula and process conditions:
[0081] Among them, the molecular weight M w In the polyether type thermoplastic polyurethane of 300K~500K (here K means unit thousand), the adding ratio is 60% (weight percentage, the same below), and the molecular weight is M w Polyether thermoplastic polyurethane at 150K~250K, adding 35%, blowing agent N 2 , The addition amount is 4.95%, the nucleating agent is carbon black, and the addition amount is 0.05%. Twin screw extruder L / D=56, screw heating temperature 160-220℃, static mixer temperature 140-180℃, melt pump inlet pressure 100-150bar, process water pressure about 6bar, controlled pressure release The difference (that is, the pressure difference between the high-pressure hot melt at the die outlet and the process water in the underwater cutting cha...
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