Process for the production of dry-spun hollow polyacrylonitrile fibers
and filaments
    1.
    发明授权
    Process for the production of dry-spun hollow polyacrylonitrile fibers and filaments 失效
    生产干纺中空聚丙烯腈纤维和细丝的方法

    公开(公告)号:US4457885A

    公开(公告)日:1984-07-03

    申请号:US461803

    申请日:1983-01-28

    摘要: Hollow acrylonitrile fibres and filaments are prepared by dry spinning the spinning dope through a nozzle having loop-shaped nozzle orifices, the solution having a viscosity equivalent to at least 120 falling ball seconds, measured at 80.degree. C., or at least 75 falling ball seconds, measured at 100.degree. C., wherein the nozzle orifice area of the profiling nozzle is smaller than 0.2 mm.sup.2 and the maximum width of the sides of the loop-shaped nozzle is 0.1 mm and the overlap between the two ends of the sides of the loop-shaped nozzle forms an angle of from 10.degree. to 30.degree. measured from the center of the nozzle and wherein the spinning air acts on the filaments in a transverse direction to the filament take-off and the air direction forms an angle of from 80.degree. to 100.degree. with a straight line passing through the opening between the sides.

    摘要翻译: 中空丙烯腈纤维和长丝通过将纺丝原液通过具有环形喷嘴孔的喷嘴进行干纺来制备,该溶液的粘度相当于在80℃下测量的至少120个落球秒,或至少75个落球 秒,在100℃下测量,其中成型喷嘴的喷嘴孔面积小于0.2mm 2,并且环形喷嘴的侧面的最大宽度为0.1mm,并且两侧的两端之间的重叠 环形喷嘴形成从喷嘴中心测量的10°至30°的角度,并且其中旋转空气沿着灯丝起飞的横向方向作用在长丝上,并且空气方向形成从 80°至100°,直线穿过两侧之间的开口。

    Process for the production of dry-spun hollow polyacrylonitrile fibers
and filaments
    3.
    发明授权
    Process for the production of dry-spun hollow polyacrylonitrile fibers and filaments 失效
    生产干纺中空聚丙烯腈纤维和细丝的方法

    公开(公告)号:US4432923A

    公开(公告)日:1984-02-21

    申请号:US386501

    申请日:1982-06-09

    摘要: Hollow polyacrylonitrile fibers having a uniform closed cavity structure are obtained by dry-spinning filament-forming acrylonitrile polymers from a solution through a spinning jet comprising annular jet bores of the type shown in FIG. 1, the solution having a viscosity of at least 120 falling-ball seconds, as measured at 80.degree. C. or of at least 75 falling-ball seconds, as measured at 100.degree. C., the ring of the annular jet bores consisting of three, preferably equally large, ring segments at a distance from one another of at most 0.2 mm, the surface area of the jet bores of the profile jet amounting to less than 0.2 mm.sup.2 and the side width of the ring segments amounting to at most 0.1 mm, the spinning air acting on the filaments transversely of the direction in which they are taken off relative to the center of the spinning jet.

    摘要翻译: 通过包含图1所示类型的环形喷射孔的纺丝喷嘴从溶液中干燥成丝的丙烯腈聚合物,获得具有均匀闭合腔结构的中空聚丙烯腈纤维。 如图1所示,该溶液在100℃下测量时具有至少120个落球秒的粘度,如在80℃或至少75个落球秒时测量的,环形射流孔的环由 三个,优选同等大的环形段,彼此距离至多0.2mm,轮廓射流的喷射孔的表面积小于0.2mm 2,环段的侧宽度至多为0.1 mm,纺丝空气在相对于纺丝喷嘴的中心离开的方向上横向于细丝。

    Dry-spun hollow polyacrylonitrile fibres and filaments and process for
the production thereof
    5.
    发明授权
    Dry-spun hollow polyacrylonitrile fibres and filaments and process for the production thereof 失效
    干纺空心聚丙烯腈纤维和长丝及其生产方法

    公开(公告)号:US4483903A

    公开(公告)日:1984-11-20

    申请号:US529652

    申请日:1983-09-06

    摘要: Hollow acrylonitrile fibres and filaments are prepared by dry spinning the spinning dope through a nozzle having loop-shaped nozzle orifices, the solution having a viscosity equivalent to at least 120 falling ball seconds, measured at 80.degree. C., or at least 75 falling ball seconds, measured at 100.degree. C., wherein the nozzle orifice area of the profiling nozzle is smaller than 0.2 mm.sup.2 and the maximum width of the sides of the loop-shaped nozzle is 0.1 mm and the overlap between the two ends of the sides of the loop-shaped nozzle forms an angle of from 10.degree. to 30.degree. measured from the center of the nozzle and wherein the spinning air acts on the filaments in a transverse direction to the filament take-off and the air direction forms an angle of from 80.degree. to 100.degree. with a straight line passing through the opening between the sides.

    摘要翻译: 中空丙烯腈纤维和长丝通过将纺丝原液通过具有环形喷嘴孔的喷嘴进行干纺来制备,该溶液的粘度相当于在80℃下测量的至少120个落球秒,或至少75个落球 秒,在100℃下测量,其中成型喷嘴的喷嘴孔面积小于0.2mm 2,并且环形喷嘴的侧面的最大宽度为0.1mm,并且两侧的两端之间的重叠 环形喷嘴形成从喷嘴中心测量的10°至30°的角度,并且其中旋转空气沿着灯丝起飞的横向方向作用在长丝上,并且空气方向形成从 80°至100°,直线穿过两侧之间的开口。

    Preparation of low residual solvent content polyacrylonitrile filaments
    6.
    发明授权
    Preparation of low residual solvent content polyacrylonitrile filaments 失效
    制备低残留溶剂含量的聚丙烯腈长丝

    公开(公告)号:US4505870A

    公开(公告)日:1985-03-19

    申请号:US505514

    申请日:1983-06-17

    IPC分类号: D01D5/04 D01F6/18 D01F6/38

    CPC分类号: D01F6/18 D01D5/04

    摘要: Polyacrylonitrile filaments having a residual solvent content of less than 5% by weight and a total linear density of over 100,000 dtex can be prepared without contact with an extracting agent for the spinning solvent by a process in which(a) the spinning solution spun has a viscosity at 100.degree. C. of 10 to 60 falling-ball seconds,(b) the filaments are treated while still hot, directly at the end of the spinning cell, inside it or immediately outside the end of the cell, with a spin-finish which contains a lubricant and an antistat and which gives the filaments a moisture content of at most 10% by weight, relative to the solids content of the fibre, and(c) the filaments are immediately exposed to a heat treatment without cooling down first.

    摘要翻译: 残留溶剂含量小于5重量%,总线密度超过100,000dtex的聚丙烯腈长丝可以通过纺丝溶液的萃取剂与纺丝溶剂的萃取剂接触而制备,其中(a)旋转纺丝溶液具有 在100℃下的粘度为10至60个落球秒,(b)长丝在仍然热的情况下直接在纺丝单元的末端处于其内部或紧邻电池端部之外, 其包含润滑剂和抗静电剂,并且相对于纤维的固体含量使细丝的水分含量为至多10重量%,和(c)长丝立即暴露于热处理而不先冷却 。

    Continuous dry-spinning process for highly shrinkable acrylonitrile
filaments and fibers
    9.
    发明授权
    Continuous dry-spinning process for highly shrinkable acrylonitrile filaments and fibers 失效
    用于高收缩丙烯腈长丝和纤维的连续干纺工艺

    公开(公告)号:US4508672A

    公开(公告)日:1985-04-02

    申请号:US505542

    申请日:1983-06-17

    IPC分类号: D01F6/18 D01F6/38 D01D5/22

    CPC分类号: D01F6/18

    摘要: Ready-for-dispatch highly shrinkable filaments and fibers made of acrylonitrile copolymers can be prepared in a continuous dry-spinning method in which:(a) the spinning solution spun has a viscosity at 100.degree. C. of 10 to 60 falling-ball seconds,(b) the evaporation of the solvent in the spinning cell is controlled in such a way that on leaving the spinning cell the solvent contact of the filaments is at most 10% by weight, relative to the solids content of the fiber,(c) before the stretch the filaments are treated with a spin-finish which contains a lubricant and an antistat and gives the filaments a moisture content of at most 10% by weight, relative to the solids content of the fiber, and(d) before or during the stretch the filaments have no contact with any other extraction liquid for the spinning solvent.

    摘要翻译: 由丙烯腈共聚物制成的高效收缩长丝和纤维可以在连续干纺法中制备,其中:(a)纺丝纺丝溶液在100℃下的粘度为10至60个落球秒 (b)纺丝细胞中溶剂的蒸发以这样一种方式进行控制,即离开纺丝细胞时纤维的溶剂接触率相对于纤维的固体含量为至多10重量%,(c )在拉伸之前,用含有润滑剂和抗静电剂的旋涂处理细丝,并且相对于纤维的固体含量使长丝具有至多10重量%的水分含量,和(d)在 在拉伸期间,丝与纺丝溶剂的任何其它提取液不接触。

    Process for spinning hydrophilic acrylic fibers with improved coloring
response to dyes
    10.
    发明授权
    Process for spinning hydrophilic acrylic fibers with improved coloring response to dyes 失效
    纺丝亲水丙烯酸纤维的方法,改善对染料的着色反应

    公开(公告)号:US4185058A

    公开(公告)日:1980-01-22

    申请号:US877318

    申请日:1978-02-13

    IPC分类号: D01F6/18 D01F8/08 B29H7/20

    CPC分类号: D01F6/18

    摘要: The invention relates to hydrophilic fibers and filaments with good coloring response to dyes from filament-forming hydrophobic synthetic polymers having a sheath-core structure with a highly microporous core and a substantially compact sheath and having a water retention capacity of at least 10% wherein the pores in the core have an average pore diameter measured in the direction of the cross-section of the fiber, of at most 4000 A. The invention relates also to a process for the production of those filaments and fibers according to a dry-spinning process wherein a spinning solution is spun below the boiling point of the spinning solvent used.

    摘要翻译: 本发明涉及具有良好着色响应的亲水纤维和长丝,其具有长丝形成疏水性合成聚合物的染料,所述疏水合成聚合物具有皮芯结构,其具有高度微孔的芯和基本上紧密的护套,并且具有至少10%的保水能力,其中 核心中的孔具有在纤维横截面方向上测量的平均孔径至多为4000。本发明还涉及根据干纺丝方法生产这些长丝和纤维的方法 其中纺丝溶液在所用纺丝溶剂的沸点以下旋转。