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CHARGE MODIFIED MICROPOROUS MEMBRANE, PROCESS FOR CHARGE MODIFYING SAID MEMBRANE, AND PROCESS FOR FILTRATION OF FLUIDS

机译:电荷修饰的微孔膜,用于修饰所述膜的电荷的过程以及流体的过滤过程

摘要

CHARGE MODIFIED MICROPOROUS MEMBRANE, PROCESSFOR CHARGE MODIFYING SAID MEMBRANE, ANDPROCESS FOR FILTRATION OF FLUIDSABSTRACTA cationic charge modified microporous membrane is provided.The membrane comprises a hydrophilic organic polymericmicroporous membrane having bonded thereto, through a cross-linking agent, a charge modifying amount of a cationic chargemodifying agent. The charge modifying agent is an aliphatic amineor polyamine, preferably tetraethylene pentamine, and the cross-linking agent is an aliphatic polyepoxide having a molecular weight ofless than about 500, preferably 1, 4 butanediol diglycidyl ether. Themicroporous membrane is preferably nylon. The process for applyingthe charge modifying agent to the membrane, preferably comprisescontacting the membrane with an aqueouos solution of the chargemodifying agent and then contacting the membrane with a substan-tially aqueous solution of the cross-linking agent. The preferredprocess uses high purity water, i.e. water having no significant ioniccontent, to produce a membrane suitable for use in filtering ultrapure (18 megohm-cm resistivity) water for use in producing electronicdevices. Such a membrane exhibits an advantageously low "flush-out"time compared to known cationic charge modified microporousmembranes and unmodified microporous membranes.
机译:充电修饰的微孔膜,过程用于修改所述膜的电荷,以及流体过滤过程抽象提供了阳离子电荷改性的微孔膜。膜包含亲水性有机聚合物通过交叉连接到其上的微孔膜连接剂,改变电荷量的阳离子电荷改性剂。电荷改性剂是脂肪族胺或多胺,最好是四亚乙基五胺,以及连接剂是分子量为小于约500,优选1,4-丁二醇二缩水甘油醚。的微孔膜优选是尼龙。申请流程膜的电荷改性剂优选包含使膜与电荷的水溶液接触改性剂,然后使膜与大量的交联剂的全部水溶液。首选该方法使用高纯度水,即没有明显离子性的水含量,以生产适用于超滤的膜用于生产电子产品的纯净水(电阻率为18兆欧·厘米)设备。这种膜表现出有利的低“冲洗”性与已知阳离子电荷改性微孔相比的时间膜和未修饰的微孔膜。

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