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Hollow fiber membrane, method for producing hollow fiber membrane, hollow fiber membrane module, membrane separation apparatus and membrane separation method

机译:中空纤维膜,生产中空纤维膜,中空纤维膜组件,膜分离装置和膜分离方法的方法

摘要

Hollow fiber membrane of hollow fiber typeThe shrinkage rate of the inner diameter of the hollow fiber membrane after 96 hours in a predetermined membrane separation method wasIt is less than 0.1% and 9% relative to the inner diameter at the start of useA predetermined membrane separation method isHollow fiber membraneFirst and second chambers partitioned with hollow fiber membranesWith a hollow fiber membrane module havingThe first liquid is fed to the first chamber at a first pressureThe second liquid is fed into the second chamber at a second pressure lower than the first pressure.The water contained in the first liquid in the first chamber is transferred to the second liquid in the second chamber through the hollow fiber membraneThe concentrated liquid, which is concentrated from the first chamber, is concentrated.The second diluent liquid diluted from the second chamber is discharged.The outer space of the hollow fiber membrane is the first chamber.The inner space of the hollow fiber membrane is the second chamber.The first pressure isThe second pressure is constant;The pressure difference between the first and second liquids is 0 MPaHollow fiber membrane.
机译:中空纤维的中空纤维膜在预定膜分离方法中96小时后,中空纤维膜的内径的收缩速率相对于USEA预定膜分离方法开始的内径小于0.1%和9%用中空纤维膜分隔的易下载纤维膜与具有第一液体的中空纤维膜模块以第一液体进料到第一腔室的第一腔室中的中空纤维膜模块以低于第一压力的第二压力进料到第二腔室中。包含的水在第一腔室中的第一液体中通过中空纤维膜在第二腔室中的第二液体转移到第二液体中,浓缩液体浓缩,浓缩。从第二腔室稀释的第二稀释剂液体排出。中空纤维膜的外部空间是第一腔室。空洞的内部空间BER膜是第二腔室。第一压力是第二压力是恒定的。第一和第二液体之间的压力差是0突出的纤维膜。

著录项

  • 公开/公告号JPWO2020175375A1

    专利类型

  • 公开/公告日2021-09-13

    原文格式PDF

  • 申请/专利权人 東洋紡株式会社;

    申请/专利号JP20210502195

  • 申请日2020-02-21

  • 分类号B01D69/08;B01D63/02;B01D69/02;B01D69;B01D71/10;B01D71/56;B01D71/68;D01D5/06;D01D5/24;

  • 国家 JP

  • 入库时间 2022-08-24 20:59:43

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