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Process for the separation of high quality biotechnologically prepared compounds by cross-flow microfiltration

机译:通过错流微滤分离高质量生物技术制备的化合物的方法

摘要

The invention relates to a process for the separation of biotechnologically produced valuable materials form a cell suspension by crossflow microfiltration to obtain an high specific permeate flux while retention stays near 0% for long periods. To enable crossflow microfiltration to be carried out on an industrial scale in biotechnology in the separation of biotechnologically produced extracellular valuable materials from a cell suspension, particularly in the separation of alkaline protease for recovering enzyme, under economically acceptacle conditions, alkaline protease of relatively high molecular weight, more especially enzyme 20,000 daltons, is separated from a fermenter solution using polysulfone tubes having micropore diameters of from 0.3 to 0.5 mu m at a rate of flow of the fermenter solution of from 3 to 6 m/s parallel to the membrane surface and with a pressure difference between the concentrate side and the permeate side of 2 bar, the ratio of the mean pore diameter of the membrane to the size of the microorganisms remaining in the concentrate being between 0.15 and 0.
机译:本发明涉及一种通过错流微滤从细胞悬液中分离出生物技术产生的有价值的物质的方法,以得到高的比渗透通量,同时保留率长期保持在0%附近。为了能够在生物技术中以工业规模进行错流微滤,以从细胞悬液中分离出生物技术产生的细胞外有价值物质,特别是在经济上可接受的条件下分离碱性蛋白酶以回收酶的情况下,使用相对较高分子的碱性蛋白酶使用具有0.3至0.5μm的微孔直径的聚砜管,以平行于膜表面的流速为3至6m / s的速率,从发酵罐溶液中分离出重量为3kg / s,更特别是> 20,000道尔顿的酶。在浓缩物侧和渗透物侧之间的压力差为2 bar的情况下,膜的平均孔径与浓缩物中剩余微生物的尺寸之比在0.15和0之间。

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