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    • 84. 发明授权
    • Apparatus for producing thermoplastic yarns
    • 用于生产热塑性纱线的装置
    • US5076773A
    • 1991-12-31
    • US442509
    • 1989-11-28
    • Paolo Bert
    • Paolo Bert
    • D01D5/08D01D5/16D01D13/00D01F6/06
    • D01F6/06D01D13/00D01D5/08D01D5/16
    • Continuous polypropylene multifilament yarns are made by melt spinning and stretching in an integral process; a sufficient number of filaments for forming at least 8 continuous filament yarns each consisting of at least 10 filaments are melt spun through a spinneret (11) at a speed of at least 400 m/min into a vertical air quenching zone or shaft (12) for solidification; the filaments are arranged to form a substantially planar array of parallel and mutually distanced yarn strands; then, the filaments are stretched to achieve substantial orientation by passing the yarn strands, while maintaining them in the array, over peripheral surface portions of a sequence of rotating cylinders (141, 142, 143, 144) having parallel axes of rotation, each strand (S) passing over surface portions along a discrete path which is substantially defined by a plane intersecting perpendicularly with the parallel axes of the cylinders; each strand is in frictional contact with the peripheral surface portions for a total contact path length of from 1000 to 6500 mm and at least 50%, preferably 75-100%, of the path length of frictional contact are provided on a total number of from 2 to 6 and preferably 4 large diameter cylinders; the yarn strands are wound as a poduct at a speed of at least 1000 m/min, e.g. at about 2000 m/min.
    • 85. 发明授权
    • Melt spinning apparatus
    • 熔纺设备
    • US5059104A
    • 1991-10-22
    • US414290
    • 1989-09-29
    • Bacchini Alberto
    • Bacchini Alberto
    • D01D4/00D01D5/08D01D5/088D01D5/092D01F6/06
    • D01D5/088D01D5/08D01F6/06
    • A melt-spinning apparatus includes a feed device for feeding a molten polymer composition from at least one extruder to a multiplicity of spinning orifices provided by a plurality of spinnerets for producing a multiplicity of discrete continuous extrudates emerging from the orifices in a generally downward direction; quenching devices for cooling the extrudates and for solidifying them to form a multiplicity of discrete continuous filaments; take-up and stretching devices provided downstream from the orifices for contacting and stretching the filaments; the quenching devices include guides for directing at least one stream of a cooling gas having a quenching temperature onto a portion, at least, of the extrudates; the orifices or spinnerets are arranged to form an annular array and a portion, at least, of the quenching devices is provided to direct the cooling gas stream in a substantially radial manner onto the extrudates that emerge from the orifices in the annular array.
    • 熔融纺丝装置包括用于将熔融聚合物组合物从至少一个挤出机供给到由多个喷丝头提供的多个纺丝孔的进料装置,用于在大体上向下的方向上产生从孔中出来的多个离散的连续挤出物; 用于冷却挤出物并固化它们以形成多个离散的连续长丝的淬火装置; 从所述孔下游提供用于接触和拉伸长丝的吸收和拉伸装置; 淬火装置包括用于将具有淬火温度的冷却气体的至少一个流引导至至少部分挤出物的引导件; 孔或喷丝头被布置成形成环形阵列,并且至少提供淬火装置的部分,以将冷却气流以基本上径向的方式引导到从环形阵列中的孔排出的挤出物上。
    • 90. 发明授权
    • Uniformly dyeable nylon 66 fiber and process for the production thereof
    • 均匀染色尼龙66纤维及其生产方法
    • US4542063A
    • 1985-09-17
    • US651646
    • 1984-09-18
    • Hiroshi TanjiMichitaka IwataHideo Sato
    • Hiroshi TanjiMichitaka IwataHideo Sato
    • D01D5/08D01D5/084D01D5/098D01F6/60D02G3/00
    • D01D5/084D01D5/08D01D5/098D01F6/60Y10T428/2913
    • A nylon 66 fiber capable of being uniformly dyed and having an initial modulus at 20.degree. C. and a relative humidity of 60% of about 15 g/d to about 65 g/d and a relationship of a peak temperature [T.sub.max (.degree.C.)] at peak of dynamic mechanical loss tangent (tan .delta.) measured with a frequency of 110 Hz and a peak value of the dynamic mechanical loss tangent [(tan .delta.).sub.max ] represented by the equation:T.sub.max (.degree.C.).ltoreq.-320(tan .delta.).sub.max +132The fiber has such a structure that refractive indices are different between an outer layer of the fiber and an inner layer of the fiber. The fiber is made by extruding a melt of nylon 66, passing the extruded filaments through a heating zone provided at the surface of the extrusion nozzle and having a length of at least about 5 cm and a temperature of about 150.degree. C. to about the melting point of the polymer, applying a suction with an aspirator located below the heating zone, and then winding at a winding speed of at least about 4,000 m/min.
    • 能够均匀染色,初始模量为20℃,相对湿度为60%约15g / d至约65g / d的尼龙66纤维和峰值温度[Tmax(℃) 。)]在以110Hz的频率测量的动态机械损耗角正切(tanδ)的峰值和由以下等式表示的动态机械损耗角正切[(tanδ)max]的峰值:Tmax(℃) / = - 320(tanδ)max + 132纤维具有纤维的外层和纤维的内层之间的折射率不同的结构。 纤维通过挤出尼龙66的熔体制成,使挤出的长丝通过设置在挤出喷嘴表面处的加热区,并且具有至少约5cm的长度和约150℃的温度至约 聚合物的熔点,用位于加热区下方的吸气器进行抽吸,然后以至少约4000m / min的卷绕速度卷绕。