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Production of crimped tows of polyacrylonitrile filamentary material

机译:聚丙烯腈丝状卷曲丝束的生产

摘要

In a continuous process for producing a crimped tow of filaments of polyacrylonitrile containing a major portion, e.g. 75 per cent by weight, of acrylonitrile combined in the polymer molecule, a dry uncrimped tow is wetted (100-700 per cent by weight of water) and heated by an aqueous fluid at a temperature of 155-205 DEG F. and is continuously fed under uniform tension (0.005-0.5 grams per denier) to and crimped within a zone which is within said temperature range. The hot crimped tow is passed, while it is relaxed, to and through a separate cooling zone in which it is cooled to a temperature below 120 DEG F. to set the crimp. The aqueous fluid may contain an "effect" agent, e.g. an anti-static material containing a low viscosity oil or a lubricant. The tow fed to the crimping zone may have a residual shrinkage of 0-3 per cent or may be pretreated to remove such shrinkage by continuous passage, FORM:0809039/IV (c)/1 in a relaxed state, through a liquid at a temperature of 210-230 DEG F. with a dwell therein of 5 seconds to 30 minutes and tensioning the tow to align the filaments thereof. Cooling may be effected by passage through air at "room" temperature or exposure to blasts, sprays or a circulation of cooling fluid during which the tow may be supported on a porous conveyer. As shown in Fig. 1, tow 10 is led from a tunnel or apron dryer 12 by an apron 14 and passed continuously through a shrinkage removal zone provided by a J-box 16 which may have, on each side at 24, alternately operating liquid sprays which deposit the tow in a spiral form 26 which is subjected, in a jacketed section 28, to a hot fluid, e.g. steam or non-solvents (in relation to the filament material) such as ethylene glycol, diethylene glycol, ethylene glycol monoethyl ether, glycerol, propylene glycol. Tow then receives the aqueous fluid treatment at a temperature of 155 DEG to 205 DEG F. in a device 60 which may be spray means or a bath in which the tow, guided by rollers, is repeatedly immersed. Tow 76, continuously crimped in a "nip-rolls and stuffer-box" apparatus and discharged on to a conveyer 80 is cooled in a J-box 84. If water is the coolant, it is removed from the tow, as by a squeeze roll, and the tow is dried or stapled, dried and opened. If dry tow is to be freed of residual shrinkage, it may be first wetted with water, e.g. by a spray, trough, tube or wiper (not shown) to facilitate subsequent handling.
机译:在生产包含主要部分例如聚丙烯酰胺的聚丙烯腈细丝的卷曲丝束的连续方法中。将75%(重量)的丙烯腈结合到聚合物分子中,将干燥的未卷曲丝束润湿(100-700%(重量)水),并用水性流体在155-205°F的温度下加热,并连续加热在均匀张力(0.005-0.5克/旦尼尔)下进料并卷曲在所述温度范围内的区域内。热卷曲的丝束在松弛的同时进入并通过一个单独的冷却区,在冷却区内将其冷却到低于120°F的温度以设定卷曲。水性流体可包含“效应”剂,例如。包含低粘度油或润滑剂的抗静电材料。送入压接区的丝束可以具有0-3%的残余收缩率,也可以通过在松弛状态下连续通过液体进行预处理,以消除这种收缩在210-230°F的温度下保持5秒至30分钟,并拉紧丝束以使其细丝对齐。冷却可通过在“室温”下通过空气或暴露于鼓风,喷雾或冷却液循环来进行,在此期间丝束可支撑在多孔输送机上。如图1所示,丝束10由胶圈14从隧道或胶圈干燥器12引出,并连续通过由J盒16提供的除皱区,该胶盒的每侧在24处可以交替工作。喷雾使丝束沉积成螺旋形26,在夹套部分28中该丝束经受热流体,例如蒸汽或非溶剂(相对于长丝材料),例如乙二醇,二甘醇,乙二醇单乙醚,甘油,丙二醇。然后,丝束在装置60中在155-205°F的温度下接受含水流体处理,该装置可以是喷雾装置或浴,该丝束在辊的引导下反复浸入其中。在“夹辊和填料箱”设备中连续卷曲并排放到输送机80上的丝束76在J盒84中冷却。如果水是冷却剂,则通过挤压将其从丝束中除去卷,然后将丝束干燥或装订,干燥并打开。如果要使干丝束没有残留的皱缩,可以先用水例如湿的丝束湿润。通过喷雾器,槽,管子或刮水器(未显示)方便后续处理。

著录项

  • 公开/公告号GB809039A

    专利类型

  • 公开/公告日1959-02-18

    原文格式PDF

  • 申请/专利权人 AMERICAN CYANAMID COMPANY;

    申请/专利号GB19560015539

  • 发明设计人

    申请日1956-05-18

  • 分类号D02G1/12;

  • 国家 GB

  • 入库时间 2022-08-23 19:48:47

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