Preparation method of thermoplastic polyurethane micro air bag elastomer material
A technology of thermoplastic polyurethane and elastomer materials, applied in chemical instruments and methods, chemical/physical/physicochemical fixed reactors, chemical/physical processes, etc., can solve problems such as high energy consumption and low yield
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[0052] A preparation method of thermoplastic polyurethane micro airbag elastomer material includes the following steps:
[0053] (1) Feeding liquid raw materials including diisocyanate molecules and polyols and solid additives into a twin-screw reactor to perform polymerization chain extension reaction to obtain a high molecular weight hot melt;
[0054] (2) Push the high molecular weight hot melt of step (1) from the outlet of the twin-screw reactor into the mixing extruder to continue the reaction to generate a polymer thermoplastic polyurethane melt with a narrow molecular weight distribution;
[0055] (3). Continue to feed the obtained polymer thermoplastic polyurethane melt into the foaming extruder. At the same time, add polymer particle auxiliary materials, nucleating agent and foaming agent to the foaming extruder to mix and distribute the materials After homogenization, the pressure is controlled and quantitatively delivered to the die by the melt booster pump, and extruded ...
Embodiment 1
[0077] According to the above as figure 1 The process flow of preparing the heat-damaged polyurethane micro airbag elastomer material of the present invention according to the following raw material formula and process conditions:
[0078] Among them, the polyol is preferably polytetrahydrofuran ether glycol with a molecular weight of 1000-2000, added in a weight ratio of 55-70%, diphenylmethane diisocyanate 20-35%, n-butanol 5-15%, hindered phenolic antioxidant ( Ciba Irganox 1010) 0.5-2%, hindered amine light stabilizer 0.5-2%, mold release agent 0.05-0.5%. The polymer chain extension reaction is carried out in a double screw reactor to produce linear polyurethane macromolecular polymers with a molecular weight of 100,000 to 500,000. The heating temperature of the twin-screw reactor is 180-240℃, and the rotating speed is 100-1500rpm; the rotating speed of the mixing extruder is 100-300rpm, and the heating temperature is 140-220℃.
[0079] Polymer excipients are molecular weight ...
Embodiment 2
[0083] According to the above as figure 1 The process flow of preparing the heat-damaged polyurethane micro airbag elastomer material of the present invention according to the following raw material formula and process conditions:
[0084] Among them, the polyol is preferably polytetrahydrofuran ether glycol with a molecular weight of about 1000, and the weight ratio is 55%, diphenylmethane diisocyanate 35%, n-butanol 5.5%, hindered phenolic antioxidant (Ciba Irganox 1010) 2%, Hindered amine light stabilizer 2%, release agent 0.5%. The polymer chain extension reaction is carried out in a twin-screw reactor to produce linear polyurethane macromolecular polymers with a molecular weight of about 300,000. The heating temperature of the twin-screw reactor is 180°C and the rotating speed is 800 rpm; the rotating speed of the mixing extruder is 100 rpm and the heating temperature is 140°C.
[0085] Polymer excipients are molecular weight M w About 80,000 polyether thermoplastic polyureth...
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