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FOULING AND CLEANING OF FORWARD OSMOSIS (FO) MEMBRANES RECYCLING A TREATED WASTEWATER

机译:回收处理过的废水中前渗透(FO)膜的污染和清洁

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Forward osmosis (FO) membranes have been used for wastewater recovery and desalination as apromising technology. This research studies the natural organic matter (NOM) fraction causingfouling on the active (AL) and support layer (SL) of a FO membrane, with the active layer facingthe feed side (AL-FS), using a secondary wastewater effluent (SWWE) as feed water, andseawater as a draw solution (DS). Liquid chromatography with organic carbon detection (LCOCD)chromatograms and fluorescence excitation-emission matrixes (F-EEM) spectra of theinitial and final DS and SWWE suggested that protein-like substances and polysaccharidespresent in the SWWE were forming a fouling layer on the AL of the FO membrane, reducing theflux of water permeating through the membrane. NOM fouling shows a 90% reversibility whenair scouring for 15 minutes within the concentrated feed water (CFW) is applied. When chemicalcleaning of the AL (Alconox solution and EDTA) was performed after the former air scouring,the flux increased by 3%, and the irreversible fouling was quantified as 8.2%. Transparentexopolymer particles (TEP) were identified on the support layer of the FO membrane in contactwith the seawater, reducing the flux of the FO membrane in ≤ 8.2% of the initial flux. Chemicalcleaning of the SL with a solution of 1% NaOCl during 10 minutes was effective in removing theTEP accumulated on the membrane.
机译:正渗透(FO)膜已被用于废水的回收和脱盐。 有前途的技术。这项研究研究了自然有机物(NOM)分数引起的 FO膜的活性层(AL)和支撑层(SL)结垢,且活性层朝向 进料侧(AL-FS),使用二级废水流出物(SWWE)作为进料水,以及 海水作为汲取溶液(DS)。带有有机碳检测的液相色谱(LCOCD) 色谱图和荧光激发发射矩阵(F-EEM)谱图 最初和最终的DS和SWWE建议蛋白质样物质和多糖 SWWE中存在的污染物正在FO膜的AL上形成结垢层,从而减少了 透过膜的水通量。 NOM结垢显示出90%的可逆性 在浓缩给水(CFW)中进行15分钟的空气精练。当化学 在之前的空气洗涤之后,对AL(Alconox溶液和EDTA)进行清洁, 通量增加了3%,​​不可逆结垢的定量值为8.2%。透明的 在FO膜的支撑层上发现了接触的外聚合物颗粒(TEP) 与海水一起使用,可将FO膜的通量降低至初始通量的≤8.2%。化学制品 在10分钟内用1%NaOCl溶液清洁SL可以有效去除 TEP累积在膜上。

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