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    • 1. 发明授权
    • Apparatus for melt mixing synthetic polymers
    • 熔融混合合成聚合物的装置
    • US5697402A
    • 1997-12-16
    • US623952
    • 1996-03-29
    • John A. HodanMatthew B. HoytOtto M. Ilg
    • John A. HodanMatthew B. HoytOtto M. Ilg
    • D01D5/28F04F5/00
    • D01D5/28B29B7/88Y10T137/2076Y10T137/212Y10T137/2147Y10T137/2158Y10T137/2218
    • A system for mixing first and second polymer melt flows and directing a mixed polymer melt flow to one and another downstream locations includes a control valve having an inlet port for receiving the first polymer melt flow, and a pair of outlet ports, and a fluidic valve for forming the mixed flow of the first and second polymer melt flows and directing the mixed flow to one of a plurality of downstream locations. The fluidic valve is provided with a primary supply port for receiving the second polymer melt flow, a pair of secondary supply ports which are fluid-connected with the primary supply port at a mixing intersection, and a plurality of discharge ports extending from the mixing intersection. Each discharge port directs the mixed flow of the first and second polymer melt flows to a respective downstream location. A pair of branch conduits is provided which fluid-connect one of the pair of outlet ports of the control valve to a respective one of the secondary supply ports of the fluidic valve.
    • 用于混合第一和第二聚合物熔体流动并将混合的聚合物熔体流引导到一个和另一个下游位置的系统包括具有用于接收第一聚合物熔体流的入口端口的控制阀和一对出口以及流体阀 用于形成第一和第二聚合物熔体流的混合流,并将混合流引导到多个下游位置之一。 流体阀设置有用于接收第二聚合物熔体流的主供应端口,在混合交叉口处与主供应端口流体连接的一对二次供应端口和从混合交叉口延伸的多个排出端口 。 每个排出口将第一和第二聚合物熔体流的混合流引导到相应的下游位置。 提供了一对分支管道,其将控制阀的一对出口端口中的一个流体连接到流体阀的相应的一个二次供应端口。
    • 2. 发明授权
    • Apparatus for melt mixing and spinning synthetic polymers
    • 用于熔融混合和纺丝合成聚合物的装置
    • US5656304A
    • 1997-08-12
    • US613581
    • 1996-03-12
    • John A. HodanMatthew B. HoytOtto M. Ilg
    • John A. HodanMatthew B. HoytOtto M. Ilg
    • D01D5/28D01D4/06
    • D01D5/28B29B7/88Y10T137/2076Y10T137/212Y10T137/2147Y10T137/2158Y10T137/2218
    • An apparatus for melt mixing and spinning synthetic polymers, which has a plurality of spinning nozzle units, a main extruder with a capacity sufficient to feed a polymer melt to the plurality of spinning nozzle units, a main metering pump for receiving the polymer melt through a conduit system from the main extruder and directing the polymer melt through a branched conduit system including a first branch and a second branch to the spinning nozzle unit, a plurality of multiple way fluidic devices, a two way valve for receiving the polymer melt from the main metering pump and for directing the polymer melt through the first branch or through the second branch and through the multiple way fluidic devices to the plurality of spinning nozzle units, thereby directing the way within the multiple way fluidic devices, a plurality of concentrate extruders for directing a plurality of concentrates through the multiple way fluidic devices to the spinning nozzle units, each of said multiple way fluidic devices thereby combining the polymer melt received from the first branch with one of the concentrates to a polymer melt mixture and directing the polymer melt mixture to one of the plurality of spinning nozzles units.
    • 一种用于熔融混合和纺丝合成聚合物的设备,其具有多个纺丝喷嘴单元,具有足以将聚合物熔体供给到多个纺丝喷嘴单元的能力的主挤出机,用于通过一个聚合物熔体接收聚合物熔体的主计量泵 导管系统,并且将聚合物熔体引导通过包括第一分支和第二分支的分支导管系统到纺丝喷嘴单元,多个多通道流体装置,用于从主体接收聚合物熔体的双向阀 计量泵并且用于将聚合物熔体引导通过第一分支或通过第二分支并且通过多通道流体装置引导到多个纺丝喷嘴单元,从而在多通道流体装置内引导多个浓缩物挤出机,用于引导 通过多路流体装置到纺丝喷嘴单元的多个浓缩物,每个所述多路流动装置 从而将从第一分支接收的聚合物熔体与其中一种浓缩物组合成聚合物熔体混合物并将聚合物熔体混合物引导到多个纺丝喷嘴单元之一。
    • 3. 发明授权
    • Process for modifying synthetic bicomponent fiber cross-sections
    • 改性合成双组分纤维截面的方法
    • US6153138A
    • 2000-11-28
    • US288185
    • 1999-04-08
    • Charles F. Helms, Jr.Otto M. IlgDiane R. KentMatthew B. HoytJohn A. Hodan
    • Charles F. Helms, Jr.Otto M. IlgDiane R. KentMatthew B. HoytJohn A. Hodan
    • D01D5/253D01F8/12B29D31/00D01D5/24D01D8/04D01D8/12
    • D01F8/12D01D5/253Y10T428/2929Y10T428/2931Y10T428/2973Y10T428/2975
    • Bicomponent fibers of different cross-sections may be formed without changing the geometry of the spinneret orifices. More specifically, at least two polymers are co-melt-spun through an orifice of fixed geometry so as to achieve a bicomponent fiber having a desired cross-section. In order to change to a bicomponent fiber having a cross-section which is different, therefore, at least one of (1) the differential relative viscosity, (2) the relative proportions of the first and/or second polymers, and (3) the cross-sectional bicomponent distribution of the first and second polymers, is changed. In such a manner, therefore, a wide variety of bicomponent fibers having different cross-sectional geometries may be produced without changing the fixed geometry orifice through which the polymers are co-melt-spun. Thus, bicomponent fiber cross-sections may be "engineered" to suit a variety of needs without necessarily shutting down production equipment in order to change spinnerets. The bicomponent fibers are most preferably multilobal (e.g., trilobal) in which the core component is generally triangularly shaped.
    • 可以在不改变喷丝孔的几何形状的情况下形成不同横截面的双组分纤维。 更具体地说,至少两种聚合物通过固定几何形状的孔进行共熔纺丝,以达到具有所需横截面的双组分纤维。 因此,为了改变具有不同截面的双组分纤维,因此,(1)差分相对粘度,(2)第一和/或第二聚合物的相对比例和(3)中的至少一个, 改变第一和第二聚合物的横截面双组分分布。 因此,以这种方式,可以生产具有不同横截面几何形状的各种各样的双组分纤维,而不改变聚合物共熔共纺的固定几何孔。 因此,双组分纤维横截面可以“工程化”以适应各种需要,而不必关闭生产设备以改变喷丝头。 双组分纤维最优选为多叶形(例如三叶形),其中芯部分通常为三角形。
    • 4. 发明授权
    • Process for melt mixing and spinning synthetic polymer
    • 熔融混合和纺丝合成聚合物的方法
    • US5651928A
    • 1997-07-29
    • US624211
    • 1996-03-29
    • John A. HodanMatthew B. HoytOtto M. Ilg
    • John A. HodanMatthew B. HoytOtto M. Ilg
    • D01D5/28D01D4/06D01F8/04
    • D01D5/28B29B7/88Y10T137/2076Y10T137/212Y10T137/2147Y10T137/2158Y10T137/2218
    • Synthetic polymers are melt-mixed and spun from a mixture of respective first and second polymer melt flows. Specifically, the mixture of first and second polymer melt flows are mixed at a fluidic mixing device having a mixing intersection which receives the first and second polymer melt flows and discharges the mixture thereof respectively into at least one or another of multiple discharge ports fluid-connected with a respective spinning nozzle. The mixed flow of first and second polymer melt flows is controlled by diverting the first polymer melt so that it (i) entirely flows along a first flow path to responsively merge with the second polymer melt flow at the mixing intersection of the mixing device and thereby cause the mixed polymer flow to be discharged through the one discharge port, or (ii) entirely flow along a second flow path to responsively merge with the second polymer melt at the mixing intersection of the mixing device and thereby cause the mixed polymer flow to be discharged through the other discharge port. The mixed polymer flow thereby diverted is thus spun by one or another of the spinning nozzles, respectively.
    • 将合成聚合物熔融混合并从各自的第一和第二聚合物熔体流的混合物纺丝。 具体地说,第一和第二聚合物熔体流动的混合物在具有接收第一和第二聚合物熔体流动的混合交叉点的流体混合装置中混合,并将其混合物分别排放到流体连接的多个排放口中的至少一个或另一个 与相应的纺丝喷嘴。 通过转移第一聚合物熔体来控制第一和第二聚合物熔体流的混合流,使得其(i)完全沿着第一流动路径流动以在混合装置的混合交叉处与第二聚合物熔体流反应地合并,从而 导致混合聚合物流通过一个排出口排出,或(ii)沿着第二流动路径全部流动,以在混合装置的混合交叉处与第二聚合物熔体反应地合并,从而使混合的聚合物流为 通过另一个排放口排出。 由此分流的混合聚合物流分别由一个或另一个纺丝喷嘴纺出。
    • 7. 发明授权
    • Continuous polymerization and direct fiber spinning and apparatus for accomplishing same
    • 连续聚合和直接纺丝纺丝及其设备
    • US06441109B1
    • 2002-08-27
    • US09475675
    • 1999-12-30
    • Dominick A. BurloneMatthew B. HoytCharles F. Helms, Jr.John A. HodanRichard KotekCarol W. MorganRandall A. SferrazzaFang A. WangOtto M. IlgTerry D. RobertsRonald G. Morrow
    • Dominick A. BurloneMatthew B. HoytCharles F. Helms, Jr.John A. HodanRichard KotekCarol W. MorganRandall A. SferrazzaFang A. WangOtto M. IlgTerry D. RobertsRonald G. Morrow
    • C08F201
    • C08G69/18D01D1/06D01F6/60
    • Continuous anionic polymerization and melt-spinning of a polycaprolactam includes forming a reaction mixture by bringing at least two streams of liquid caprolactam respectively containing a polymerization initiator and co-initiator into contact with one another, and then subjecting the reaction mixture to anionic polymerization reaction conditions to obtain a molten polycaprolactam. The molten polycaprolactam is the directly (i.e., without intermediate solidification) transferred to, and extruded through, a fiber-forming orifice of a spinneret to form a fiber thereof. One exemplary system to achieve such continuous anionic polymerization and melt-spinning of polycaprolactam includes a mixer for receiving and mixing at least two streams of liquid caprolactam respectively containing a polymerization initiator and co-initiator, and a reactor and melt-spinning apparatus downstream of the mixer. The reactor and melt-spinning apparatus most preferably is formed of multiple plates which establish a reactor zone having a flow path for the reaction mixture which is sized and configured to achieve a predetermined residence time of the reaction mixture therein, and a temperature control zone in thermal communication with the reactor plate for controlling the temperature of the reaction plate to achieve anionic polymerization reaction conditions while the reaction mixture is flowing along the defined flow path therein to obtain the molten polycaprolactam. A spinneret zone downstream of the reactor zone thus receives the molten polycaprolactam directly and forms a fiber therefrom by extruding it through the spinneret's fiber-spinning orifice.
    • 聚己内酰胺的连续阴离子聚合和熔融纺丝包括通过使至少两股分别含有聚合引发剂和共引发剂的液体己内酰胺流彼此接触形成反应混合物,然后将反应混合物进行阴离子聚合反应条件 得到熔融的聚己内酰胺。 熔融的聚己内酰胺直接(即没有中间凝固)转移到喷丝板的纤维形成孔中并被挤出,以形成其纤维。 实现这种连续阴离子聚合和聚己内酰胺的熔融纺丝的一个示例性系统包括用于接收和混合分别含有聚合引发剂和共引发剂的至少两种液体己内酰胺流的混合器,以及在聚合引发剂和共引发剂下游的反应器和熔融纺丝装置 混合器。 反应器和熔体纺丝装置最优选地由多个板形成,该板形成具有反应混合物流动路径的反应器区,该反应器区的尺寸和构造被设计成达到其中反应混合物的预定停留时间,以及温度控制区 与反应器板的热连通,用于控制反应板的温度以实现阴离子聚合反应条件,同时反应混合物沿其中限定的流动路径流动以获得熔融的聚己内酰胺。 因此,反应器区域下游的喷丝头区域直接接收熔融的聚己内酰胺并通过将其通过喷丝头的纤维纺丝孔口挤出而形成纤维。
    • 8. 发明授权
    • Process for modifying synthetic bicomponent fiber cross-sections and
bicomponent fibers thereby produced
    • 用于改性由此制备的合成双组分纤维横截面和双组分纤维的方法
    • US5948528A
    • 1999-09-07
    • US980232
    • 1997-11-28
    • Charles F. Helms, Jr.Otto M. IlgDiane R. KentMatthew B. HoytJohn A. Hodan
    • Charles F. Helms, Jr.Otto M. IlgDiane R. KentMatthew B. HoytJohn A. Hodan
    • D01D5/253D01F8/12D02G3/00
    • D01F8/12D01D5/253Y10T428/2929Y10T428/2931Y10T428/2973Y10T428/2975
    • Bicomponent fibers of different cross-sections may be formed without changing the geometry of the spinneret orifices. More specifically, at least two polymers are co-melt-spun through an orifice of fixed geometry so as to achieve a bicomponent fiber having a desired cross-section. In order to change to a bicomponent fiber having a cross-section which is different, therefore, at least one of (1) the differential relative viscosity, (2) the relative proportions of the first and/or second polymers, and (3) the cross-sectional bicomponent distribution of the first and second polymers, is changed. In such a manner, therefore, a wide variety of bicomponent fibers having different cross-sectional geometries may be produced without changing the fixed geometry orifice through which the polymers are co-melt-spun. Thus, bicomponent fiber cross-sections may be "engineered" to suit a variety of needs without necessarily shutting down production equipment in order to change spinnerets. The bicomponent fibers are most preferably multilobal (e.g., trilobal) in which the core component is generally triangularly shaped.
    • 可以在不改变喷丝孔的几何形状的情况下形成不同横截面的双组分纤维。 更具体地说,至少两种聚合物通过固定几何形状的孔进行共熔纺丝,以达到具有所需横截面的双组分纤维。 因此,为了改变具有不同截面的双组分纤维,因此,(1)差分相对粘度,(2)第一和/或第二聚合物的相对比例和(3)中的至少一个, 改变第一和第二聚合物的横截面双组分分布。 因此,以这种方式,可以生产具有不同横截面几何形状的各种各样的双组分纤维,而不改变聚合物共熔共纺的固定几何孔。 因此,双组分纤维横截面可以“工程化”以适应各种需要,而不必关闭生产设备以改变喷丝头。 双组分纤维最优选为多叶形(例如三叶形),其中芯部分通常为三角形。