首页> 外国专利> Production of ultra-pure water involves passing water through biofilter followed by dosing with biostatic agent before passing through reverse osmosis membrane filter to reduce total organic carbon content efficiently without biofouling

Production of ultra-pure water involves passing water through biofilter followed by dosing with biostatic agent before passing through reverse osmosis membrane filter to reduce total organic carbon content efficiently without biofouling

机译:超纯水的生产涉及使水通过生物滤池,然后在通过反渗透膜滤池之前先添加生物抑制剂,以有效降低总有机碳含量,而不会造成生物积垢。

摘要

To produce an ultra-pure water, the water inflow is passed to a bioreactor (2), followed by a non-oxidizing processing stage with a biostatic action, and a final membrane filter. To produce an ultra-pure water, the water inflow is passed to a bioreactor (2), followed by a non-oxidizing processing stage with a biostatic action, and a final membrane filter. The final membrane filter (8) has a reverse osmosis action. Heavy metal compounds are added to the water in the biostatic processing stage (6), preferably copper salts and/or zinc salts, fed in together. The biological matter turnover is registered between the biostatic processing and the final stages, to set the processing actions. The water is filtered at the bioreaction stage. The water from the bioreactor is passed through an adsorption stage (5) using active carbon, before or after the biostatic processing stage. Before the water is passed into the bioreactor, it passes through a flocking and sedimentation stage. An independent claim is included for a water purification assembly with a bioreactor and especially a multiple-layer filter (2), which is cleaned by back flushing. A following dosing unit (6) adds a heavy metal biostatic agent, with a final reverse osmosis membrane filter (8). Preferred Features: A biofouling monitor (9) in front of the membrane filter measures the level of infection in the water by a germ count, to set the working of the dosing stage (6). A monitor after the bioreactor measures the assimilable organic matter (AOC) in the water, to determine the back flushing cycles of the bioreactor. An adsorber (5) is downstream of the bioreactor. A flocking and sedimentation stage (1) is in front of the bioreactor (2).
机译:为了产生超纯水,将流入的水通入生物反应器(2),然后进行具有生物活性的非氧化处理阶段,最后进行膜过滤。为了产生超纯水,将流入的水通入生物反应器(2),然后进行具有生物活性的非氧化处理阶段,最后进行膜过滤。最终的膜滤器(8)具有反渗透作用。在生物静力处理阶段(6)中,将重金属化合物,优选铜盐和/或锌盐一起加入水中。在生物静态处理和最终阶段之间记录生物物质周转,以设置处理动作。在生物反应阶段将水过滤。在生物静态处理阶段之前或之后,使来自生物反应器的水通过使用活性炭的吸附阶段(5)。在水进入生物反应器之前,它会经过植绒和沉淀阶段。包括具有生物反应器,尤其是多层过滤器(2)的水净化组件的独立权利要求,其通过反冲洗进行清洁。后续的计量单元(6)添加了重金属生物抑制剂,并带有最终的反渗透膜过滤器(8)。首选功能:膜滤器前面的生物污损监测器(9)通过细菌计数来测量水中的感染水平,以设定加料阶段(6)的工作状态。生物反应器后的监测器测量水中的可吸收有机物(AOC),以确定生物反应器的反冲洗周期。吸附器(5)在生物反应器的下游。植绒沉淀阶段(1)在生物反应器(2)的前面。

著录项

  • 公开/公告号DE10015453A1

    专利类型

  • 公开/公告日2001-10-31

    原文格式PDF

  • 申请/专利权人 STEAG ENCOTEC GMBH;

    申请/专利号DE2000115453

  • 发明设计人

    申请日2000-03-29

  • 分类号C02F3/00;C02F1/44;C02F9/00;

  • 国家 DE

  • 入库时间 2022-08-22 01:09:51

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