首页> 外国专利> Producing polyurethane fibers for emission of light over surface of fibers, comprises producing fibers from basic material of polyurethane by extruding, and cooling extruded fibers in cooling zones and then subjecting to stretching process

Producing polyurethane fibers for emission of light over surface of fibers, comprises producing fibers from basic material of polyurethane by extruding, and cooling extruded fibers in cooling zones and then subjecting to stretching process

机译:生产用于在纤维表面上发光的聚氨酯纤维,包括通过挤出由聚氨酯的基础材料生产纤维,并在冷却区域中冷却挤出的纤维,然后进行拉伸过程。

摘要

The method comprises producing fibers from a basic material of polyurethane by extruding, where the basic material has residual moisture of below 0.02% before extrusion, adjusting the temperature and mass pressure of the extrusion on three positions along an extrusion cylinder, and cooling the extruded fibers in several cooling zones (30, 40) and then subjecting to a stretching process. The temperature adjusted along the cylinder lies between a glass transition temperature and a melting point of an extruding material and the highest value of the temperature is adjusted in an entrance area. The method comprises producing fibers from a basic material of polyurethane by extruding, where the basic material has residual moisture of below 0.02% before extrusion, adjusting the temperature and mass pressure of the extrusion on three positions along an extrusion cylinder, and cooling the extruded fibers in several cooling zones (30, 40) and then subjecting to a stretching process. The temperature adjusted along the cylinder lies between a glass transition temperature and a melting point of an extruding material and the highest value of the temperature is adjusted in an entrance area of an extruder screw. The mass temperature of the extruding material is as in the range of its melting temperature but not deviates more than 40 K from the melting temperature. The extruded fibers are cooled in a first cooling zone with a cooling media temperature below the glass transition temperature, and are cooled in the first cooling zone with an inlet temperature of highly 40 K below the melting temperature not under the glass transition temperature. The extruded fibers are cooled in a second cooling zone in a second medium with a cooling media temperature below the glass transition temperature. The extruded fibers are cooled up to below the glass transition temperature. The adjustment of the extruded fiber is carried out by stretching the fiber in the progression of the first cooling step at a temperature of the fiber above the glass transition temperature. The optical characteristics of the fiber are determined by the specific mass output of the extruder (20), are adjusted by different cylinder zone temperatures and are adjusted by the stretching process. An independent claim is included for a device for producing polyurethane fibers for the emission of light over a surface of the fibers.
机译:该方法包括通过挤出由聚氨酯的基础材料生产纤维,其中该基础材料在挤出之前具有低于0.02%的残留水分;在沿着挤出筒的三个位置上调节挤出的温度和质量压力;以及冷却挤出的纤维。在几个冷却区(30、40)中进行拉伸处理。沿着圆柱体调节的温度在玻璃化转变温度和挤出材料的熔点之间,并且在入口区域调节温度的最高值。该方法包括通过挤出由聚氨酯的基础材料生产纤维,其中该基础材料在挤出之前具有低于0.02%的残留水分;在沿着挤出筒的三个位置上调节挤出的温度和质量压力;以及冷却挤出的纤维。在几个冷却区(30、40)中进行拉伸处理。沿圆筒调节的温度在玻璃化转变温度和挤出材料的熔点之间,并且在挤出机螺杆的入口区域中调节温度的最高值。挤出材料的质量温度在其熔融温度的范围内,但与熔融温度的偏差不超过40K。挤出的纤维在第一冷却区中以低于玻璃化转变温度的冷却介质温度进行冷却,并且在第一冷却区中以比熔融温度高40 K的入口温度进行冷却,而不是在玻璃化转变温度以下。挤出的纤维在第二介质中的第二冷却区中以低于玻璃化转变温度的冷却介质温度进行冷却。将挤出的纤维冷却至低于玻璃化转变温度。通过在第一冷却步骤的过程中在高于玻璃化转变温度的纤维温度下拉伸纤维来进行挤出纤维的调节。纤维的光学特性由挤出机(20)的比重输出确定,由不同的圆筒区温度调节,并由拉伸过程调节。包括用于生产聚氨酯纤维的装置的独立权利要求,所述聚氨酯纤维用于在纤维的表面上发光。

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