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Improvements in the melt spinning of fine denier synthetic filament yarn

机译:细旦合成长丝纱线熔纺的改进

摘要

PICT:0661999/IV (a)/1 Fine denier filament yarns are obtained by melt spinning a synthetic polymeric substance through a multihole spinneret into a stream of inert gas passing through a spinning cell and maintained at a temperature sufficient to cool the molten substance to below its solidification temperature so as to form a plurality of fine denier filaments which are gathered together to form a yarn and steadied by means of a convergence yarn guide as soon as the filaments solidify and become substantially non-tacky. The fine denier filament yarns are those in the range of 3.0-1.0 or lower denier per filament. Preferably, air or other gas is passed as a cooling medium across the path of the moving filamentary material adjacent the spinneret. The convergence guide serves to minimize the effects of any pulsations in the cooling medium as well as any momentary tension fluctuations occasioned by the take-up mechanism. The yarn from the convergence guide may pass through the cell to a second guide and thence to a conditioning apparatus. As shown, filaments are melt-spun through spinneret 4 and gathered together to form a yarn 5 by means of convergence guide 6. The spinning cell 7 is provided with means, not shown, for passing a current of cooling fluid in non-turbulent manner at right-angles to the direction of travel of the filaments, e.g. it may be constructed as described in Specification 533,304. The yarn passes to another guide 8, then through a moisture-conditioning chamber 9, and finally to a wind-up device. In an example, polyhexamethylene adipamide is melted and maintained at 285 DEG C. in an atmosphere of nitrogen. The molten polymer is pumped through a filter pack comprising sand layers and screens and then through a spinneret with 70 holes, each of diameter 0.0009 inch. A cross-flow cooling chamber is placed 1 inch below the base of the spinneret. The filaments solidify at about 21 inches from the spinneret and at this point they are brought together as a yarn by passing through a thread guide. The process is applicable to the production of yarns of polyamides, polyesters, polyethers, polyacetals, polyester-polyamides, polyethylenes, polyvinyl compounds, polystyrene, and polyacrylates. Specifications 471,590 and 577,436 also are referred to.
机译:细旦长丝纱线是通过将合成高分子物质通过多孔喷丝板熔融纺丝成惰性气体流而制成的,该惰性气体流通过纺丝室并保持在足以冷却熔融金属的温度下当纤维凝固到低于其凝固温度时,以形成许多细旦尼尔的细丝,这些细旦的细丝聚集在一起以形成纱线,并且一旦细丝凝固并且基本上不发粘,就借助于会聚纱线导引器将其稳定。细旦长丝纱线是在每根长丝3.0-1.0或更低的范围内的那些。优选地,空气或其他气体作为冷却介质通过邻近喷丝板的移动丝状材料的路径。收敛引导件用于使冷却介质中的任何脉动以及卷取机构引起的任何瞬时张力波动的影响最小化。来自会聚引导件的纱线可穿过单元到达第二引导件,然后到达调节装置。如图所示,长丝通过喷丝头4熔融纺丝,并通过会聚导纱器6聚集在一起以形成纱线5。纺丝室7设有未示出的装置,用于使冷却流体流以非湍流方式通过。与细丝的行进方向成直角,例如它可以按照规范533,304中的描述进行构造。纱线到达另一个导纱器8,然后穿过湿度调节室9,最后到达卷绕装置。在一个实例中,将聚六亚甲基己二酰胺熔化并在氮气氛下保持在285℃。熔融的聚合物被泵送通过包括砂层和筛子的滤袋,然后被泵送通过具有70个孔的喷丝板,每个孔的直径为0.0009英寸。横流式冷却室位于喷丝板底部下方1英寸处。长丝在距喷丝头约21英寸处凝固,这时长丝通过导丝器而成为纱线。该方法适用于生产聚酰胺,聚酯,聚醚,聚缩醛,聚酯-聚酰胺,聚乙烯,聚乙烯基化合物,聚苯乙烯和聚丙烯酸酯的纱线。还参考了规格471,590和577,436。

著录项

  • 公开/公告号GB661999A

    专利类型

  • 公开/公告日1951-11-28

    原文格式PDF

  • 申请/专利权人 IMPERIAL CHEMICAL INDUSTRIES LIMITED;

    申请/专利号GB19490013976

  • 发明设计人

    申请日1949-05-25

  • 分类号D01D5/08;

  • 国家 GB

  • 入库时间 2022-08-24 01:03:08

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