Extrusion foaming thermoplastic polyurethane elastomer bead and preparation method thereof
A thermoplastic polyurethane, extrusion foaming technology, applied in the field of foaming materials, can solve problems such as environmental pollution, high cost, and complicated foaming process, and achieve the effects of no environmental pollution, stable quality, and uniform density distribution
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[0027] For the preparation of raw material thermoplastic polyurethane elastomer particles: it is usually produced by mixing isocyanate, an active hydrogen compound with a molar mass of 500-10000g / mol and a chain extender with a molar mass of 50-500g / mol, and a catalyst is added during production; The following examples describe preferred starting materials for the production of thermoplastic polyurethane particles in the present invention:
[0028] Isocyanates include aliphatic, cycloaliphatic, aromatic and araliphatic; diisocyanates such as toluene diisocyanate (TDI), diphenylmethane-2,2'-, 2,4'- or 4,4'-diisocyanate are preferred Isocyanate (MDI), 3-isocyanatomethylene-3,5,5-trimethylcyclohexylisocyanate (IPDI), hexamethylene diisocyanate (HDI), dicyclohexylmethane diisocyanate (HMDI), 1 ,5-Naphthalene diisocyanate (NDI), p-phenylene diisocyanate (PPDI), 1,4-cyclohexane diisocyanate (CHDI), cyclohexane dimethylene diisocyanate (HXDI), particularly preferably diphenylmethane ...
Embodiment 1
[0035] Example 1, 100Kg of thermoplastic polyurethane (TPU) particles A shown in Table 1, 0.5Kg of talc, and 0.05Kg of antioxidant 1010 were mixed evenly, and then the above mixture was put into an extruder to granulate to obtain foamable Particles, the above-mentioned particles are finally put into a single-stage single-screw extruder, the extrusion speed of the material is controlled at 80Kg per hour, the injection speed of supercritical carbon dioxide is controlled at 0.8Kg per hour, the die head pressure is 1Mpa, and the die head temperature The water temperature of the underwater pelletizer is controlled at 70°C; the material can be continuously added according to the above-mentioned component ratio for continuous production, and the foaming density of the pellets obtained is 0.306g / cm 3 .
Embodiment 2
[0036]Example 2, 100Kg of thermoplastic polyurethane (TPU) particles B shown in Table 1, 0.01Kg of talc, and 0.2Kg of antioxidant 1010 were mixed evenly, and then the above mixture was put into an extruder to granulate to obtain foamable Particle, above-mentioned particle is dropped into single-stage single-screw extruder at last, and the extruding speed of material is controlled at extruding 55Kg per hour, and the injection speed of supercritical nitrogen is controlled at 6Kg per hour, and die head pressure is 12Mpa, and die head temperature is 185°C, the water temperature of the underwater pelletizer is controlled at 70°C; materials can be added continuously according to the above-mentioned component ratio for continuous production, and the foaming density of the obtained particles is 0.208g / cm 3 .
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