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    • 55. 发明授权
    • Degradable monofilament and preparation process thereof
    • 可降解单丝及其制备方法
    • US6090910A
    • 2000-07-18
    • US984538
    • 1997-12-03
    • Hosei ShinodaMasanobu Ajioka
    • Hosei ShinodaMasanobu Ajioka
    • A61L17/12D01F6/84C08G63/08A61L17/00C08G63/88D02J1/22
    • D01F6/84A61L17/12
    • A degradable copolymer filament comprising an internal structure having the following separate phases: (a) a matrix phase comprised as a primary component of a polymer segment which exhibits a tensile Young's modulus of 2 GPa or less and a strength retention of 50% or more after two weeks in water at 37.degree. C., pH 7.3, and (b) a micro-dispersed phase comprised as a primary component of a polymer segment which exhibits a tensile strength of 200 MPa or more and a strength reduction greater than the matrix phase in water at 37.degree. C., pH 7.3. The weight ratio of each component in the matrix phase and dispersed phase is 50:50 to 95:5, respectively, and the dispersed phase a needle structure oriented by stretching in the fiber direction. A degradable monofilament having an excellent mechanical strength and flexibility, moderate hydrolyzability, high ligature stability and being suitable as a material of surgical absorbable suture can be obtained. A preparation process is also provided.
    • 一种可降解共聚物长丝,其包含具有以下分离相的内部结构:(a)基质相,其包含作为聚合物链段的主要组分,其显示出2GPa或更小的拉伸杨氏模量和50%以上的强度保持率 在37℃,pH7.3的水中两周,和(b)包含作为聚合物链段的主要组分的微分散相,其表现出200MPa或更大的拉伸强度,并且强度降低大于基体相 在37℃,pH 7.3的水中。 基体相和分散相中各成分的重量比分别为50:50〜95:5,分散相为沿纤维方向拉伸取向的针状结构。 可以获得具有优异的机械强度和柔韧性,适度的水解性,高韧带稳定性并且适合作为手术可吸收缝合材料的可降解单丝。 还提供了一个准备过程。
    • 60. 发明授权
    • Industrial process for the separation and recovery of chlorine
    • 用于分离和回收氯的工业过程
    • US5254323A
    • 1993-10-19
    • US921606
    • 1992-08-03
    • Hiroyuki ItohYoshitsugu KonoIsao KikuchiShinji TakenakaMasanobu AjiokaMitsuo Kudoh
    • Hiroyuki ItohYoshitsugu KonoIsao KikuchiShinji TakenakaMasanobu AjiokaMitsuo Kudoh
    • C01B7/07C01B7/01B01D53/34
    • C01B7/0743
    • A gaseous mixture containing chlorine, carbon dioxide and non-condensable gas is compressed and cooled to separate it into a residual gas formed principally of a major portion of the non-condensable gas and a condensate formed primarily of chlorine. The condensate is fed to a stripping column to desorb carbon dioxide and a minor portion of the non-condensable gas dissolved in the condensate. The stripped gas formed primarily of chlorine and carbon dioxide may be treated further. Namely, the stripped gas is mixed with the residual gas. At least a portion of the mixed gas is fed into an absorption column, whereby a major portion of remaining chlorine is absorbed to lower the chlorine content Removal of chlorine from such a gaseous mixture or an off-gas from the above process can be achieved by washing it with an aqueous solution or suspension containing an alkali metal sulfite and/or an alkaline earth metal sulfite while controlling the pH of the solution or suspension within a range of 1.9-6.3.
    • 将含有氯,二氧化碳和不可冷凝气体的气体混合物压缩并冷却,将其分离成主要由不可冷凝气体主要形成的残留气体和主要由氯气形成的冷凝物。 将冷凝物供入汽提塔以解吸二氧化碳和少部分溶解在冷凝物中的不可冷凝气体。 主要由氯和二氧化碳形成的汽提气体可以进一步处理。 即,将汽提的气体与残留气体混合。 将混合气体的至少一部分进料到吸收塔中,从而吸收主要部分的剩余氯以降低氯含量从上述方法从这种气体混合物或废气中除去氯可以通过 用包含碱金属亚硫酸盐和/或碱土金属亚硫酸盐的水溶液或悬浮液洗涤,同时将溶液或悬浮液的pH控制在1.9-6.3的范围内。