Highly-transparent polyurethane hot-melt film applicable to sandwich glass and preparation method thereof
A polyurethane hot-melt and hot-melt film technology, applied in polyurea/polyurethane adhesives, chemical instruments and methods, glass/slag layered products, etc., can solve problems such as failure to use adhesives, and achieve easy control and production The effect of simple process and good adhesion
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Embodiment 1
[0032] 100Kg of polytetrahydrofuran diol with a molecular weight of 2000 and 50Kg of polyoxypropylene diol with a molecular weight of 2000 were dehydrated under vacuum at 120°C for 2 hours to make the moisture content less than 0.05%.
[0033] Mix the above-mentioned just dehydrated polyol mixture with 0.8Kg catalyst (a mixture of 0.4Kg dibutyltin dilaurate and 0.4Kg triethylamine), 1Kg antioxidant 1010, 1Kg optical stabilizer UV328, and then mix it with 34Kg MDI flows continuously into the twin-screw extruder for mixing and reaction at a ratio of 4.5:1. When the material flows through the middle of the extruder, start to add the dehydrated mixed chain extender at a ratio of 10:1 of the actual flow rate. agent (7Kg methylpropanediol, 7Kg1,6-hexanediol), 2.4Kg coupling agent KH560, 0.8Kg catalyst (mixture of 0.4Kg dibutyltin dilaurate and 0.4Kg triethylamine), screw speed 70 rev / The temperature in the feeding zone is 120°C, the temperature in the reaction zone is 190°C, and th...
Embodiment 2
[0035] 176Kg of polytetrahydrofuran diol with a molecular weight of 2000 was vacuum dehydrated at 120°C for 2 hours to make the moisture content less than 0.05%.
[0036] Mix the above-mentioned freshly dehydrated polyol mixture with 0.8Kg catalyst (a mixture of 0.4Kg dibutyltin dilaurate and 0.4Kg triethylamine), 1Kg antioxidant 245, 1Kg optical stabilizer UV9, and then mix it with 20Kg IPDI flows continuously into the twin-screw extruder for mixing and reaction at a ratio of 8.8:1. When the material flows through the middle of the extruder, add the dehydrated mixed chain extender at a ratio of 37.8:1 of the actual flow rate. agent (1Kg methylpropanediol and 2Kg 1,6-hexanediol), 2Kg coupling agent KH550, 0.2Kg catalyst (mixture of 0.1Kg dibutyltin dilaurate and 0.1Kg triethylamine), screw speed 80 rpm The temperature in the feeding zone is 120°C, the temperature in the reaction zone is 170°C, and the temperature in the extrusion zone is 190°C. Finally, it is extruded, cooled...
Embodiment 3
[0038] 80Kg of polyoxypropylene diol with a molecular weight of 1000 was vacuum dehydrated at 120° C. for 2 hours to make the moisture content less than 0.05%.
[0039]Mix the above-mentioned just dehydrated polyol mixture with 0.8Kg catalyst (a mixture of 0.4Kg dibutyltin dilaurate and 0.4Kg triethylamine), 2Kg antioxidant 1010, 2Kg optical stabilizer UV327, and then mix it with 66Kg HDI continuously flows into the twin-screw extruder for mixing and reaction at a ratio of 1.28:1. When the material flows through the middle of the extruder, start to add the dehydrated mixed chain extender ( 4Kg methylpropanediol and 36Kg dipropylene glycol), 9Kg coupling agent A-172, 0.2Kg catalyzer (the mixed solution of 0.1Kg dibutyltin dilaurate and 0.1Kg triethylamine), screw speed 80 revs / min, feed intake The zone temperature is 110°C, the reaction zone temperature is 180°C, and the extrusion zone temperature is 190°C. Finally, it is extruded, cooled and granulated for later use, and the ...
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