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    • 13. 发明授权
    • Process and apparatus for the production of very fine mineral fibers, in
particular glass fibers
    • 生产非常细的矿物纤维,特别是玻璃纤维的方法和设备
    • US4838917A
    • 1989-06-13
    • US150682
    • 1988-02-01
    • Wolfram WagnerRoger NyssenDirk BerkenhausHans-Theo van Pey
    • Wolfram WagnerRoger NyssenDirk BerkenhausHans-Theo van Pey
    • C03B37/06
    • C03B37/06
    • The streams of melt issuing from the melt outlet apertures (18) at the bottom of a melting crucible (14) are broken up into fibers in a drawing nozzle by means of a blast medium directed substantially parallel to the streams of melt. The blast medium is produced by a pressure gradient in the drawing nozzle and sucked in at the drawing nozzle inlet (7). In the drawing nozzle (16), the flow velocity is reduced in a downstream diffuser after the drawing process. The blast medium is supplied in the form of a hot gas between the underside of the crucible and the top edge (15) of the drawing nozzle from opposite broadsides of the melt distributor (14) in excess to the total quantity of gas stream sucked in at the drawing nozzle inlet (7). The hot gas consists of a mixture of combustion gases and air and is at a temperature from 600.degree. C. to 1500.degree. C., preferably from 800.degree. C. to 1400.degree. C. The flow velocity of the hot gas is adjusted to a value below 100 m/s, preferably 50 m/s, in the region (13) between the drawing nozzle (16) and the melt distributor (14). Gas burners (1) provided for producing the hot gas are arranged with their combustion chambers (3) situated laterally between the melt distributor (14) and the top edge (15) of the debiteuse. The combustion chambers (3) are connected by bores (6) to air chambers which are under an excess pressure. In the combustion chambers (3), the combustion gases are homogeneously mixed with the air introduced.
    • 从熔融坩埚(14)底部的熔体出口孔(18)发出的熔体流通过基本上平行于熔体流定向的鼓风介质在拉丝喷嘴中分解成纤维。 鼓风介质由拉伸喷嘴中的压力梯度产生,并在抽吸喷嘴入口(7)处吸入。 在绘图喷嘴(16)中,拉伸处理后的下游扩散器中的流速减小。 鼓风介质以坩埚的下侧和拉丝喷嘴的顶边(15)之间的热气体的形式从熔体分配器(14)的相对的宽边提供,超过吸入的气流的总量 在绘图喷嘴入口(7)处。 热气体由燃烧气体和空气的混合物组成,温度为600℃至1500℃,优选为800℃至1400℃。将热气体的流速调节至 在拉伸喷嘴(16)和熔体分配器(14)之间的区域(13)中的值低于100m / s,优选为50m / s。 设置用于产生热气体的气体燃烧器(1)被布置成其燃烧室(3)横向位于熔体分配器(14)和脱盐槽的顶部边缘(15)之间。 燃烧室(3)通过孔(6)连接到处于过大压力下的空气室。 在燃烧室(3)中,燃烧气体与引入的空气均匀混合。
    • 18. 发明授权
    • Method for the multi-stage fibre cables and the apparatus required for it
    • 多级光纤电缆及其所需设备的方法
    • US4701980A
    • 1987-10-27
    • US847798
    • 1986-04-03
    • Wolfgang BackerWolfram WagnerGunther HahnRalf Miessen
    • Wolfgang BackerWolfram WagnerGunther HahnRalf Miessen
    • D01G1/00D02G1/12D02G1/20D06B21/00
    • D02G1/12D02G1/20
    • An improved method for the after-treatment of washed and dried fibre cable having a minimum mass of 250 ktex by crimping, fixing, cooling and optionally cutting or tearing is achieved in that the band width of the cable issuing from the drier with a covering density of at most 5 ktex/cm is reduced by at least 50% of the original band width with a corresponding increase in the packing density, is crimped in a stuffer box crimping means at a stuffer box pressure of from 4 to 10 N/cm and a stuffer box temperature of from 80.degree. to 95.degree. C., the crimping is fixed in or immediately after the stuffer box, the cable is deposited on the surface of an air-permeable conveyor belt, air is blown or sucked there through fibre package or conveyor belt and the cable is then optionally supplied to a tearing converter or a cutting machine.
    • 实现了通过压接,固定,冷却和任选地切割或撕裂使具有最小质量为250ktex的洗涤和干燥的纤维电缆的后处理的改进方法,其中从具有覆盖密度的干燥器发出的电缆的带宽 至少5ktex / cm的原始带宽的至少50%,相应地增加包装密度,在填充箱压接装置中以4至10N / cm的填塞箱压力卷曲;以及 填塞箱温度为80℃〜95℃,压片固定在填塞箱内或紧靠填料箱后,电缆沉积在透气性输送带表面,空气通过纤维包装吹入或吸入 或输送带,然后可选地将电缆提供给撕裂转换器或切割机。
    • 20. 发明授权
    • Method and device for manufacturing ultrafine fibres from thermoplastic
polymers
    • 从热塑性聚合物制造超细纤维的方法和装置
    • US5260003A
    • 1993-11-09
    • US910344
    • 1992-07-22
    • Peter R. NyssenArmin KreimerWolfram WagnerDirk Berkenhaus
    • Peter R. NyssenArmin KreimerWolfram WagnerDirk Berkenhaus
    • D01D4/02D01D5/098D04H1/56B29B9/10
    • D04H3/16D01D4/025D01D5/0985
    • A process and device for manufacturing ultrafine fibers and ultrafine-fibre mats from thermoplastic polymers with mean fibre diameters of 0,2-15 .mu.m, preferably 0,5-10 .mu.m, by a melt blowing technique. The polymer melt (12) flows through at least one bore (15) in a melt blowing nozzle (18). Immediately on emerging from the bore, gas is blown against the extrusion from both sides of the bore exit (15), thus breaking up the melt to form fibers. To this end, the gas is accelerated to supersonic speed in Laval nozzles (25, 26; 31, 32), disposed in mirror symmetry round the bore exits (15), and decelerated to just below the speed of sound in channels (27) with constant cross-section, or a cross-section which decreases in the direction of flow, fitted downstream of the Laval nozzles, and the melt (12) fed into the gas stream emerging from the channels (27).
    • PCT No.PCT / EP91 / 02152 Sec。 371日期:1992年7月22日 102(e)日期1992年7月22日PCT 1991年11月15日PCT PCT。 出版物WO92 / 10599 日期1992年6月25日。一种通过熔喷技术从平均纤维直径为0.2-15μm,优选为0.5-10μm的热塑性聚合物制造超细纤维和超细纤维垫的方法和装置 。 聚合物熔体(12)流过熔喷嘴(18)中的至少一个孔(15)。 立即从孔中出来时,气体从孔出口(15)的两侧吹向挤压件,从而将熔体分解成纤维。 为此,气体在拉瓦尔喷嘴(25,26; 31,32)中被加速到超音速,以孔对角度的方式设置在孔出口(15)周围,并且减速到正好低于通道(27)中的声速, 具有恒定的横截面,或者安装在拉瓦尔喷嘴下游的流动方向上减小的横截面,以及馈送到从通道(27)排出的气流中的熔体(12)。