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method and device for the production of a ausgeschrumpften dry kunstseidefadens

机译:于生产澳大利亚干干昆士兰淡啤酒的方法和设备

摘要

PICT:0665114/IV (a)/1 PICT:0665114/IV (a)/2 A process for the manufacture of a fully shrunk artificial thread comprises leading the thread through a drying device so that the thread can sag exclusively under the influence of its own weight, maintaining the supply speed at a constant value, and passing the thread through a discharge device rotating at constant speed and having a conical supporting face so that the position of the thread on the discharge device controls the discharge speed, the process being characterized by the provision of a guiding surface which makes an angle, preferably of 45 degrees, with the horizontal plane, which controls the position of the thread upon the discharge device and which, if moving, moves only in the direction of the movement of the thread. The thread in the drying device should hang entirely free under a tension of not more than 1 g. per 100 denier and preferably not more than 0.2 g. per 100 denier. The thread may be pre-dried to about 70 per cent moisture calculated on the dry substance before applying the process. The drying device may be heated by hot air or other gases, infra-red radiation or by dielectric heating. After leaving the discharge device the thread may be taken up by a device which can operate independently of its speed such as a ring twister or centrifuge. As shown, the dry thread 1 leaves the drying device and is discharged by a pair of rollers 2, 3, the lower roller 2 having its axis horizontal. A PICT:0665114/IV (a)/3 PICT:0665114/IV (a)/4 PICT:0665114/IV (a)/5 thread guide 4 in the form of a smooth straight-sided fork with prongs 5 and 6 forming a slot open at the top is provided between the rollers and the drying chamber. The slot is disposed in the plane parallel to that containing the roller axes with its open end upwardly inclined toward the smaller end of the rollers, and makes an angle of 45 degrees with the horizontal. The speed of rollers 2, 3 is such that the thread forms a tangent to the edges of the thread guide when it is running in the centre of the pulling-off rollers (the equilibrium position). Increasing shrinkage causes the thread to travel to the smaller side of the rollers and decreasing tension toward the larger side. If desired, the thread may lap the prongs or not even touch them in its equilibrium position. Figs. 4 and 5 show a combined drying chamber and discharge device according to the invention. The wet thread, pre-dried to 70 per cent moisture if desired, is supplied by rollers 7 and 8 at constant speed and sags under its own weight into a vertically-arranged drying channel 9 provided at the bottom with a polished plate 10 arranged preferably at 45 degrees to the horizontal. The sagging thread lightly touches this plate. The rollers 7 and 8 are arranged so that the thread enters the drying channel at the edge nearest to the upper edge of the plate. Conical rollers 2 and 3 take-up the thread, roller 2 having its axis horizontal and being disposed to the left of the supply rollers when seen in the direction of the thread entering the supply device. The dimensions and speed of the discharge rollers are such that the peripheral speed at the middle is equal to the average speed of the fully shrunk thread. If, owing to a decrease in shrinkage the loop lengthens and travels down the plate 10, the position of the thread on the discharge roller 2 is shifted toward the larger end of the rollers, and vice versa. To avoid disturbance of the loop by air currents during drying, a partition extending almost to the plate 10 may be provided, thus dividing the channel into two parts, one for the descending thread and one for the ascending thread. To enable the device to be started up the partition does not extend to the back of the channel but forms a slot therewith. Its lower edge forms a sloping slot with the plate 10. If desired (Fig. 8), the sloping surface may be the surface of one of the take-up rollers. The sagging thread, in a vertical plane, comes from the drying chamber (not shown) and is taken up by rollers 2 and 3, roller 2 having its axis 21 running parallel to the plane of the thread and forming an angle b (preferably 45 degrees) with the horizontal. As before, the speed of the rollers is such that the fully shrunk thread runs over the middle of the discharge device. Guides 11 may be provided in all embodiments to limit the sideways movement of the thread. Specification 369,669, [Group IX], is referred to.
机译: 制造完全收缩的人造线的方法包括使线穿过干燥装置,以使线可以仅下垂在其自重的影响下,将供给速度保持在恒定值,并使线穿过以恒定速度旋转并具有圆锥形支撑面的出线装置,从而使线在出线装置上的位置控制出线速度所述方法的特征在于,提供引导表面,该引导表面与水平面成角度,优选为45度,该引导表面控制线在排出装置上的位置,并且如果移动,则仅沿方向移动。线程的运动。干燥装置中的线应在不超过1 g的张力下完全自由悬挂。每100旦尼尔,优选不超过0.2g。每100旦。在应用该工艺之前,可以将线预干燥至以干物质计算的约70%的水分。干燥装置可以通过热空气或其他气体,红外线辐射或通过介电加热来加热。在离开排出装置之后,线可以被可以独立于其速度操作的装置(例如,捻线机或离心机)吸收。如图所示,干线1离开干燥装置并由一对辊2、3排出,下部辊2的轴线水平。 光滑的直叉形导线槽4在滚筒和干燥室之间设有尖头5和6,尖头5和6在顶部形成一个开口。狭槽设置在与包含滚子轴线的平面平行的平面中,其开口端朝着滚子的较小端向上倾斜,并且与水平方向成45度角。辊2、3的速度是这样的,即当线在引出辊的中心(平衡位置)上运动时,线与线引导件的边缘相切。收缩率的增加会导致线行进到辊的较小侧,而张力会朝较大侧减小。如果需要的话,线可以搭在尖头上,甚至在其平衡位置不碰尖头。无花果图4和图5示出了根据本发明的组合的干燥室和排出装置。如果需要,将预干燥至70%水分的湿丝以恒定的速度由辊7和8供给,并在其自重下垂到垂直布置的干燥通道9中,该干燥通道9的底部设有抛光板10与水平线成45度角。下垂的螺纹轻轻地接触到该板。布置辊7和8,使得线在最靠近板的上边缘的边缘处进入干燥通道。锥形辊2和3收紧线,辊2的轴线是水平的,并且在从线进入供给装置的方向看时设置在供给辊的左侧。排出辊的尺寸和速度应使中间的圆周速度等于完全收缩的线的平均速度。如果由于收缩率的减小而使线圈拉长并沿着板10行进,则排出辊2上的线的位置朝着辊的较大端移动,反之亦然。为了避免在干燥过程中气流对环的干扰,可以提供几乎延伸到板10的隔板,从而将通道分成两部分,一个用于下降线,一个用于上升线。为了使设备能够启动,分区不延伸到通道的后面,而是与通道一起形成插槽。它的下边缘与板10形成一个倾斜的缝隙。如果需要(图8),则倾斜的表面可以是卷纸辊之一的表面。垂线在垂直平面上来自干燥室(未示出),并由辊子2和3吸收,辊子2的轴线21平行于线的平面并形成角度b(最好为45度)度)。如前所述,辊子的速度应使完全收缩的线在排出装置的中部延伸。在所有实施例中可以设置引导件11以限制线的侧向运动。参考规范369,669,[IX组]。

著录项

  • 公开/公告号DE000000839243B

    专利类型

  • 公开/公告日1952-05-19

    原文格式PDF

  • 申请/专利权人 ODERZOEKINGSINST RES NV;

    申请/专利号DEP0017631D

  • 发明设计人 DIJK PIETER VAN;

    申请日1948-10-09

  • 分类号

  • 国家 DE

  • 入库时间 2022-08-24 01:17:56

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