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    • 3. 发明授权
    • Process for the purification of glucosaminoglucans
    • 葡聚糖葡聚糖纯化方法
    • US4507205A
    • 1985-03-26
    • US237880
    • 1981-02-25
    • Pietro CremonesiGiancarlo Sportoletti
    • Pietro CremonesiGiancarlo Sportoletti
    • C08B37/10B01D13/00
    • C08B37/0075
    • A process for the removal of components having low or no anticoagulant activity from a glucosaminoglucan is described which comprises subjecting said glucosaminoglucan in the form of a salt in an aqueous solution to flow across a membrane suitable for ultrafiltration, hyperfiltration (inverse osmosis) or dialysis with partial passage through said membrane, whereby fractions of low activity go through the membrane and fractions of higher activity do not go through the membrane and are concentrated. The membrane suitable for ultrafiltration may have a nominal molecular cut-off between 1000 and 15,000. The membrane suitable for dialysis may have a nominal molecular cut-off at less than 30,000. The glucosaminoglucan may be heparin in the form of the sodium or calcuium salt.
    • 描述了从葡糖淀粉葡聚糖中除去具有低或不具有抗凝血活性的成分的方法,其包括使所述水溶液中盐形式的葡糖胺葡聚糖流过适于超滤,超滤(反渗透)或透析的膜 部分通过所述膜,其中低活性部分通过膜,较高活性的级分不通过膜并且被浓缩。 适用于超滤的膜可能具有1000至15,000之间的标称分子截止值。 适用于透析的膜可能具有小于30,000的标称分子截止值。 葡糖胺葡聚糖可以是钠或钙盐形式的肝素。
    • 10. 发明授权
    • Method for the preparation of calcium heparinate
    • 方法制备肝素钙
    • US4409103A
    • 1983-10-11
    • US176861
    • 1980-08-11
    • Pietro CremonesiGiancarlo Sportoletti
    • Pietro CremonesiGiancarlo Sportoletti
    • C08B37/10B01D13/00
    • C08B37/0075
    • A process for the preparation of the calcium salt of heparin containing an amount of sodium by weight not in excess of 0.1% and containing an amount of calcium by weight not less than 9.5% is described, which comprises subjecting a solution of sodium heparinate to dialysis, hyperfiltration (inverse osmosis) or ultrafiltration by means of a semi-permeable membrane and isolating the calcium heparinate with anticoagulant activity essentially equal to the anticoagulant activity of the sodium heparinate. For the ultrafiltration, a membrane may be used in the form of a planar sheet or a membrane in the form of a spiral or "needle" having a molecular nominal cut-off at 20,000 Dalton. For the hyperfiltration (inverse osmosis), a membrane may be used having a rejection of sodium ion between 0 and 75%. For the dialysis, a membrane may be used in the form of multiple sheets or a coiled tube or hollow fibers. A plurality of dialyzers in series or in parallel is used. The process may be carried out continuously or discontinuously.
    • 描述了一种制备含有不超过0.1%重量的钠含量不超过9.5%的肝素钙盐的方法,其包括使肝素钠溶液透析 ,通过半透膜超滤(反渗透)或超滤,并分离具有基本上等于肝素钠的抗凝血活性的抗凝血活性的肝素钙。 对于超滤,膜可以以螺旋形式的平面片或膜的形式使用,或者具有20,000道尔顿的分子标称截止值的“针”形式。 对于超滤(反渗透),可以使用具有0至75%的钠离子排斥的膜。 对于透析,膜可以以多张片或螺旋管或中空纤维的形式使用。 使用多个串联或并联的透析器。 该过程可以连续地或不连续地进行。