Polyketone yarn and a method of manufacturing same
    2.
    发明授权
    Polyketone yarn and a method of manufacturing same 失效
    聚酮纱线及其制造方法

    公开(公告)号:US5552218A

    公开(公告)日:1996-09-03

    申请号:US360703

    申请日:1994-12-21

    摘要: The invention relates to polyketone yarns of which the maximum tangential modulus at an elongation of more than 0.2% is at least 10 N/tex which display both high strength and, if so desired, a high elongation at break. The quality number, which is measured on a single filament out of a bundle of at least about 30 filaments spun simultaneously through one spinneret and given as .sigma...epsilon., is higher than 85 mN/tex, preferably higher than 100 mN/tex. The quality number of a yarn spun through one spinneret of one or more holes is higher than 110 mN/tex, preferably higher than 120 mN/tex. The yarns are manufactured by extruding a solution of a linear polymer of alternating ethylene and carbon monoxide units in a resorcinol-containing solvent, after which the solvent is removed with the aid of methanol as coagulant.

    摘要翻译: PCT No.PCT / EP93 / 01586 Sec。 371日期1994年12月21日 102(e)1994年12月21日日期PCT 1993年6月21日PCT公布。 出版物WO94 / 00623 日本1994年1月6日本发明涉及聚酮纱线,其伸长率大于0.2%时的最大切向模量为至少10N / tex,其显示出高强度,如果需要,其断裂伸长率高。 质量数量是通过一根喷丝头同时纺丝的一束至少约30根细丝的单根细丝上测量的,并以西格玛的形式给出。 ε高于85mN / tex,优选高于100mN / tex。 通过一个或多个孔的一个喷丝头纺丝的纱线的质量数目高于110mN / tex,优选高于120mN / tex。 通过在含间苯二酚的溶剂中挤出交替的乙烯和一氧化碳单元的线性聚合物的溶液来制造纱线,然后借助于甲醇作为凝结剂除去溶剂。

    Process for making polyketone fibers
    3.
    发明授权
    Process for making polyketone fibers 失效
    制造聚酮纤维的方法

    公开(公告)号:US5194210A

    公开(公告)日:1993-03-16

    申请号:US694630

    申请日:1991-05-02

    CPC分类号: D01F6/30

    摘要: Fibers of an alternating carbon monoxide-ethylene polymer having a molecular weight of at least 100,000 g/mole and a birefringence of at least 650.times.10.sup.-4 can be formed by first extruding a solution of the polymer in a mixed solvent system comprising an aromatic alcohol which is free of alkyl substituents on the aromatic nucleus and another solvent which is a liquid and is other than an aromatic alcohol. The extrusion into the solvent is at an extrusion rate of at least 1 m/min and forms a solvent-containing article which is then cooled or coagulated in a non-solvent for the polymer. The solvent is removed by extraction with a non-solvent for the polymer which is soluble in the mixture of solvents and the resulting article is drawn at a temperature of at least 180.degree. C.

    摘要翻译: 分子量至少为100,000克/摩尔,双折射率至少为650×10-4的交替一氧化碳 - 乙烯聚合物的纤维可以通过首先将聚合物溶液挤出到包括芳族醇的混合溶剂体系中来形成, 在芳族核上不含烷基取代基,另一种溶剂是液体,而不是芳族醇。 挤出到溶剂中的挤出速率为至少1m / min,形成含溶剂的制品,然后将其在用于聚合物的非溶剂中冷却或凝结。 通过用可溶于溶剂混合物的聚合物的非溶剂萃取除去溶剂,并将所得制品在至少180℃的温度下拉伸。