Continuous polymerization and direct fiber spinning and apparatus for accomplishing same
    3.
    发明授权
    Continuous polymerization and direct fiber spinning and apparatus for accomplishing same 有权
    连续聚合和直接纺丝纺丝及其设备

    公开(公告)号:US06441109B1

    公开(公告)日:2002-08-27

    申请号:US09475675

    申请日:1999-12-30

    IPC分类号: C08F201

    CPC分类号: C08G69/18 D01D1/06 D01F6/60

    摘要: 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.

    摘要翻译: 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。

    High modulus polyamide fibers
    4.
    发明申请
    High modulus polyamide fibers 失效
    高模量聚酰胺纤维

    公开(公告)号:US20070210482A1

    公开(公告)日:2007-09-13

    申请号:US11528701

    申请日:2006-09-27

    IPC分类号: D01D5/06 D01F6/60

    摘要: A process for preparing high initial modulus and high tensile strength polyamide fibers is described. The process comprises complexing the polyamide with a Lewis acid, dry-jet wet spinning the complexed fibers, drying the spun fibers for a period of time, drawing the fibers, and soaking the fibers in solvent to remove the. Lewis acid. High molecular weight nylon 6,6 fibers prepared according to the described process show initial moduli of up to 30.1 GPa and tenacities of up to 2.5 GPa.

    摘要翻译: 描述了制备高初始模量和高抗拉强度聚酰胺纤维的方法。 该方法包括将聚酰胺与路易斯酸络合,干式喷射湿法纺丝复合纤维,干燥纺丝纤维一段时间,拉伸纤维,并将纤维浸泡在溶剂中以除去。 路易斯酸。 根据所述方法制备的高分子量尼龙6,6纤维显示高达30.1GPa的初始模量和高达2.5GPa的强度。

    High modulus polyamide fibers
    6.
    发明授权
    High modulus polyamide fibers 失效
    高模量聚酰胺纤维

    公开(公告)号:US07666499B2

    公开(公告)日:2010-02-23

    申请号:US11528701

    申请日:2006-09-27

    IPC分类号: D02G3/00

    摘要: A process for preparing high initial modulus and high tensile strength polyamide fibers is described. The process comprises complexing the polyamide with a Lewis acid, dry-jet wet spinning the complexed fibers, drying the spun fibers for a period of time, drawing the fibers, and soaking the fibers in solvent to remove the Lewis acid. High molecular weight nylon 6,6 fibers prepared according to the described process show initial moduli of up to 30.1 GPa and tenacities of up to 2.5 GPa.

    摘要翻译: 描述了制备高初始模量和高抗拉强度聚酰胺纤维的方法。 该方法包括将聚酰胺与路易斯酸络合,干式喷射湿法纺丝复合纤维,干燥纺丝纤维一段时间,拉伸纤维,并将纤维浸泡在溶剂中以除去路易斯酸。 根据所述方法制备的高分子量尼龙6,6纤维显示高达30.1GPa的初始模量和高达2.5GPa的强度。

    Process of making highly oriented and crystalline thermoplastic filaments
    10.
    发明授权
    Process of making highly oriented and crystalline thermoplastic filaments 有权
    制备高取向和结晶的热塑性长丝的方法

    公开(公告)号:US09080258B2

    公开(公告)日:2015-07-14

    申请号:US13383076

    申请日:2010-07-09

    摘要: A melt-spun highly oriented and crystalline thermoplastic filament or fiber having a tenacity of at least about 10 g/d, an elongation less than about 15-%, and a modulus of at least about 130 g/d. A method of making highly oriented and crystalline thermoplastic filaments has been developed that comprises extruding a thermoplastic polymer to form at least one molten filament. The at least one molten filament is introduced into a horizontal liquid isothermal bath. The bath is maintained at a temperature between the glass transition temperature and the melting temperature of the thermoplastic polymer. The bath increases the tension along the molten filament to form at least one partially oriented and low crystalline filament. The partially oriented filament is drawn to form the highly oriented and crystalline filament.

    摘要翻译: 熔体高取向和结晶的热塑性长丝或纤维,其强度为至少约10g / d,伸长率小于约15%,模量为至少约130g / d。 已经开发了制备高取向和结晶热塑性长丝的方法,其包括挤出热塑性聚合物以形成至少一种熔融长丝。 将至少一根熔融长丝引入水平液体等温浴中。 浴保持在玻璃化转变温度和热塑性聚合物的熔融温度之间的温度。 该浴增加了沿着熔融长丝的张力,以形成至少一个局部取向和低结晶长丝。 拉伸部分取向的长丝以形成高取向和结晶的长丝。