首页> 外国专利> APPARATUS FOR AUTOMATICALLY CONVERTING OPERATION MODE OF PRESSURE-DRIVEN FILM BASED ON WATER QUALITY INFORMATION AND METHOD THEREOF

APPARATUS FOR AUTOMATICALLY CONVERTING OPERATION MODE OF PRESSURE-DRIVEN FILM BASED ON WATER QUALITY INFORMATION AND METHOD THEREOF

机译:基于水质信息的压力驱动膜自动转换运行模式的装置及其方法

摘要

PURPOSE: An apparatus and a method for automatically switching the operational mode of a pressurizing film are provided to effectively control the contamination of the film and to improve energy efficiency. CONSTITUTION: A feed water storing bath(T1) stores feed water. A mixing bath(T2) mixes the feed water and coagulating chemicals to form micro flocs. A coagulating bath(T3) forms coarse flocs based on the feed water with the micro flocs. A settling bath(T4) settles the coagulated flocs. A film-based water bath(T5) receives supernatant water from the settling bath. A separating film(110) is operated based on an all filtering mode and a circulation filtering mode and treats the feed water from the film-based water bath. A backwashing bath(T6) is installed between the separating film and the film-based water bath and stores backwashing water. A pressurizing pump(P1) pressurizes water from the film-based water bath to the separating film. A treated water bath(T7) stores treated water from the separating film and supplies the backwashing water. A backwashing pump(P2) supplies the treated water as the backwashing water to the separating film in case of a back washing operation. A compressor(P3) supplies compressed air to the separating film in case of the backwashing operation. A measuring unit, a turbidity meter, a thermometer measures the chlorophyll-a, the turbidity, and the temperature of the feed water. An automatic controlling computer controls the apparatus based on the quality of the feed water.
机译:目的:提供一种用于自动切换加压膜的操作模式的装置和方法,以有效地控制膜的污染并提高能量效率。组成:给水储槽(T1)存储给水。混合浴(T2)将给水和凝结的化学品混合,形成微絮凝物。凝结浴(T3)基于与微小絮凝物的给水形成粗絮状物。沉降浴(T4)沉降凝结的絮凝物。膜基水浴(T5)从沉降浴接收上清水。分离膜(110)基于全过滤模式和循环过滤模式运行,并处理来自膜基水浴的给水。在分离膜和基于膜的水浴之间安装有回洗槽(T6),并存储回洗水。加压泵(P1)将水从膜基水浴加压到分离膜。处理后的水浴(T7)储存来自隔离膜的处理后的水,并提供反洗水。在进行反洗操作的情况下,反洗泵(P2)将处理后的水作为反洗水供应给分离膜。在进行反冲洗操作时,压缩机(P3)将压缩空气供应到隔离膜。测量单元,浊度计,温度计可测量叶绿素-a,浊度和给水温度。自动控制计算机根据给水的质量控制设备。

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