Transparent high-elasticity thermoplastic polyurethane and method of producing the same
A thermoplastic polyurethane and high-elasticity technology, applied in the field of transparent high-elasticity thermoplastic polyurethane and its preparation, can solve problems such as numerous intermediate processes and complex production processes, and achieve the effects of easy control, simple production process, good transparency and elasticity
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[0024] The preparation method of transparent high-elasticity thermoplastic polyurethane of the present invention comprises the following sequential steps:
[0025] (1) Dehydration of polyether polyols
[0026] Vacuum dehydrate the polyether polyol at 110-130°C for 1.5-2.5 hours, so that the moisture content of the polyol is less than 0.05%;
[0027] (2) The mixture obtained in step 1 is mixed in proportion with isocyanate, part catalyst, antioxidant, anti-yellowing agent, etc.;
[0028] (3) The mixture obtained in step 2 enters the extruder, and the remaining catalyst, small molecule chain extender and filler are added in the second zone of the extruder to continue the reaction and extrude.
[0029] The mixture enters the extruder after high-speed stirring. The extruder is a twin-screw extruder with a length-to-diameter ratio of 64:1. The reaction time of the material in the extruder is 0.5-5min, and the reaction temperature is 150-200°C. The temperature setting of the extru...
Embodiment 1
[0035] 2000g of polytetrahydrofuran diol was vacuum dehydrated at 120°C for 2h to make the moisture content less than 0.05%.
[0036] Put the above mixture together with 500.48g MDI, 0.25g dibutyltin dilaurate, 0.25g triethylamine, 1.0g1010, 1.0gUV327 into the high-speed mixing head, and add 20g nano TiO at the same time 2 , the particle size is 5-10nm, at a speed of not less than 3000r / min, especially 3500r / min, stirring for 0.5-1min, so that the mixture continuously flows into the extruder for reaction.
[0037]The extruder is a twin-screw extruder with a length-to-diameter ratio of 64:1 and a reaction temperature of 150-200°C. The control temperatures of the extruder section are: 90±5°C for the first zone and 150±5°C for the second zone , the third zone 170±5℃, the fourth zone 175±5℃, the fifth zone 180±5℃, the sixth zone 180±5℃, the seventh zone 180±5℃, the eighth zone 180±5℃, the Zone 9 180±5℃, Zone 10 180±5℃, Zone 11 180±5℃, Zone 12 180±5℃, Zone 13 180±5℃, Zone 14 185±5...
Embodiment 2
[0039] 2000g of polyoxypropylene diol was vacuum dehydrated at 120°C for 2h to make the moisture content less than 0.05%.
[0040] Put the above mixture together with 348.24g of TDI, 0.25g of dibutyltin dilaurate, 0.25g of triethylenediamine, 1.0g of 1076, 1.0g of UV531, 1.0g of talcum powder, etc. into the high-speed mixing head, and stir at a speed of 3500r / min for 0.5 min, so that the mixture continuously flows into the extruder for reaction, the control temperature of the extruder section is: 90±5°C, 150±5°C, 170±5°C, 175±5°C, 180±5°C, 180±5°C ℃, 180±5℃, 180±5℃, 180±5℃, 180±5℃, 180±5℃, 180±5℃, 180±5℃, 185±5℃, 175±5℃, 165±5℃ ℃, when the material flows through the second zone, start to add 62.07g ethylene glycol, 0.25g dibutyltin dilaurate, and 0.25g triethylenediamine according to the flow ratio, and the time for the material to flow through the extruder is 2.5min. The required time is 10 minutes, and the mixture of ethylene glycol, dibutyltin dilaurate and triethylenediam...
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