首页> 外国专利> Producing thread having individual filaments, by guiding each of individual filaments at distance from each other, and coating each individual filament with flowable resin having solvent and crosslinked under effect of physical variable

Producing thread having individual filaments, by guiding each of individual filaments at distance from each other, and coating each individual filament with flowable resin having solvent and crosslinked under effect of physical variable

机译:通过将每根单丝彼此隔开一段距离地引导,并在每根单丝上涂上具有溶剂并在物理变量的作用下交联的可流动树脂,生产具有单丝的线

摘要

The method for producing a thread (2'), which includes individual filaments (45, 46, 47), comprises guiding each of the individual filaments at a distance from each other, coating each of the individual filaments with a flowable resin (14) containing a solvent and crosslinked under the effect of a physical variable and/or a chemical substance, and subsequently compacting the coated individual filaments, so that a composite is formed which consists of the individual filaments and the resin cohesively surrounding the filaments and which is free of gas pockets. The method for producing a thread (2'), which includes individual filaments (45, 46, 47), comprises guiding each of the individual filaments at a distance from each other, coating each of the individual filaments with a flowable resin (14) containing a solvent and crosslinked under the effect of a physical variable and/or a chemical substance, and subsequently compacting the coated individual filaments, so that a composite is formed which consists of the individual filaments and the resin cohesively surrounding the filaments and which is free of gas pockets. The solvent contained in the resin is expelled from the composite during a drying process. The composite present as a monofilament thread is wound in an uncrosslinked state of the resin. All of the individual filaments are unidirectionally aligned during all the preceding process steps. The individual filaments are coated in a bath of the resin by immersion, where the individual filaments are continuously pulled through the bath. The compacting step takes place in a nozzle, by which the coated individual filaments are pulled, where an inner space of the nozzle is in truncated cone form, so that the surplus resin from an opening cross-section of the nozzle is held back into the inner space of the nozzle during discharging the compacted individual filaments. The individual filaments comprise one of the filament types such as para-aramide filament, carbon filament, glass filament, basalt filament and steel filament. The individual filaments have a diameter of 6-10 mu m, the compacted composite has a diameter of 250 mu m to 1.0 mm and/or the dried monofilament thread has a diameter of 220 mu m to 0.9 mm. The monofilament thread is made of a number of individual filaments with intervals of 200-1000. The resin contains water portion 30-40% before drying. The solvent is expelled from the coated and compacted composite using convection with positively promoted air and/or infrared radiation and/or microwave radiation, where the temperature is kept at 80-100[deg] C during drying process. The individual filaments are heated at 60-70[deg] C before coating with the resin. A first type of individual filaments is present in an inner zone (42) of the compacted composite of the individual filaments, a second type of the individual filaments is radially outwardly present in a first outer zone (43) subsequent to the inner zone and a third type of the individual filaments is optionally radially outwardly present in a second outer zone (44) as in the first outer zone, where the second outer zone is subsequent to the first outer zone and the boundaries between the zones are formed by cylindrical surfaces, which are coaxially directed to a thread longitudinal axis. The individual filaments are washed in a bath of a cleaning liquid before coating and/or are provided with a coating conveying the resin flow, where the individual filaments are separately guided during cleaning. Independent claims are included for: (1) a device for producing a thread; and (2) a thread.
机译:包括单个细丝(45、46、47)的生产线(2')的方法包括:引导每个单个细丝彼此相距一定距离;用可流动的树脂(14)涂覆每个单个细丝。包含溶剂并在物理变量和/或化学物质的作用下交联,然后压紧涂覆的单根细丝,从而形成复合材料,该复合材料由单根细丝和粘结性地围绕细丝的树脂组成并且是游离的气袋。包括单个细丝(45、46、47)的生产线(2')的方法包括:引导每个单个细丝彼此相距一定距离;用可流动的树脂(14)涂覆每个单个细丝。包含溶剂并在物理变量和/或化学物质的作用下交联,然后压紧涂覆的单根细丝,从而形成复合材料,该复合材料由单根细丝和粘结性地围绕细丝的树脂组成并且是游离的气袋。在干燥过程中,树脂中包含的溶剂从复合材料中排出。以单丝线形式存在的复合材料以树脂的未交联状态缠绕。在所有前面的处理步骤中,所有单个细丝都单向对齐。通过浸渍将单根长丝涂覆在树脂浴中,其中将单根长丝连续拉动通过浴。压实步骤在喷嘴中进行,通过喷嘴将涂覆的单丝拉出,喷嘴的内部空间呈圆锥台形,以便将多余的树脂从喷嘴的开口横截面保留回喷嘴中。在排出压实的单根细丝时喷嘴的内部空间。各个长丝包括长丝类型之一,例如对位芳族聚酰胺长丝,碳长丝,玻璃长丝,玄武岩长丝和钢长丝。各个长丝的直径为6-10μm,压实的复合物的直径为250μm至1.0mm,和/或干燥的单丝线的直径为220μm至0.9mm。单丝线由间隔为200-1000的多根单丝制成。在干燥之前,树脂包含30-40%的水部分。使用对流与正向促进的空气和/或红外辐射和/或微波辐射将溶剂从涂覆并压实的复合材料中排出,其中在干燥过程中将温度保持在80-100℃。在用树脂涂覆之前,将各个细丝加热至60-70℃。第一类型的单根细丝存在于单个细丝的压实复合材料的内部区域(42)中,第二种类型的单根细丝在径向上向外存在于内部区域之后的第一外部区域(43)中,并且与第一外部区域中一样,第三类型的单个细丝可选地径向向外存在于第二外部区域(44)中,其中第二外部区域在第一外部区域之后,并且区域之间的边界由圆柱表面形成;它们同轴地指向螺纹纵轴。在涂覆之前,将单根长丝在清洁液的浴中洗涤和/或设置有输送树脂流的涂层,其中在清洁过程中分别引导单根长丝。包括以下独立权利要求:(1)一种生产线的装置; (2)一个线程。

著录项

  • 公开/公告号DE102009019500A1

    专利类型

  • 公开/公告日2011-08-04

    原文格式PDF

  • 申请/专利权人 KNAPPE FAISAL H.-J.;

    申请/专利号DE20091019500

  • 发明设计人 KNAPPE FAISAL H.-J.;

    申请日2009-05-04

  • 分类号D02G3/04;

  • 国家 DE

  • 入库时间 2022-08-21 17:47:54

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