首页> 外国专利> Operational manner of the converse permeation film plant, having the computer reading possible storage, and storage for that, the converse permeation film plant null which

Operational manner of the converse permeation film plant, having the computer reading possible storage, and storage for that, the converse permeation film plant null which

机译:逆渗透膜设备的操作方式,具有计算机读取可能的存储空间,并且为此存储的逆渗透膜设备无效

摘要

PROBLEM TO BE SOLVED: To most adequately execute the production and operation of a plant by predicting the membrane transfer parameter indicting the membrane performance of a reverse osmosis membrane from the actually measured value of the operation parameter of a reverse osmosis membrane plant in accordance with the concentration polarization equation derived from a concentration polarization model and determining operating conditions in accordance with the predicted value. SOLUTION: In the reverse osmosis membrane (RO) plant, the solvent in a permeated material is permeated through the RO membrane by a pressure difference and the solute is permeated through the RO membrane by a concentration difference. In such a case, a mass transfer coefficient k is determined according to a mass transfer correlation equation (Sh=a.Reb.Scc) indicating the relation between a Sherwood number Sh, Reynolds number Re and Schmidt number Sc. The mass transfer coefficient k is substituted in the concentration polarization equation derived from the concentration polarization model in accordance with the material balance of the solute permeation, by which a membrane surface concentration Cm is determined. Next, the memberane transfer parameter expressing the membrane performance of the reverse osmosis membrane is predicted from the actually measured value of the operation parameter of the reverse osmosis membrane plant and the operation conditions of the plant are determined from the predicted value.
机译:解决的问题:根据反渗透膜工厂的运行参数的实际测量值,通过预测膜传递参数来预测反渗透膜的膜性能,从而最充分地执行工厂的生产和运营。从浓度极化模型导出浓度极化方程,并根据预测值确定运行条件。解决方案:在反渗透膜(RO)工厂中,渗透材料中的溶剂通过压力差渗透通过RO膜,而溶质通过浓度差通过RO膜渗透。在这种情况下,根据表示舍伍德数Sh,雷诺数Re和施密特数Sc之间的关系的传质相关方程式(Sh = a.Reb.Scc)来确定传质系数k。根据溶质渗透的材料平衡,将传质系数k代入从浓度极化模型导出的浓度极化方程中,由此确定膜表面浓度Cm。接下来,根据反渗透膜设备的运行参数的实际测量值来预测表示反渗透膜的膜性能的会员烷转移参数,并根据该预测值来确定设备的运行条件。

著录项

  • 公开/公告号JP3520906B2

    专利类型

  • 公开/公告日2004-04-19

    原文格式PDF

  • 申请/专利权人 東レ株式会社;

    申请/专利号JP19990241592

  • 发明设计人 谷口 雅英;中西 貴之;木原 正浩;

    申请日1999-08-27

  • 分类号B01D61/02;B01D61/12;B01D61/58;

  • 国家 JP

  • 入库时间 2022-08-21 23:24:59

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