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Desalination of brackish groundwater and reuse of wastewater by forward osmosis coupled with nanofiltration for draw solution recovery

机译:通过正渗透结合纳米过滤对咸淡水进行脱盐和废水回用以回收溶液

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This study evaluates a treatment system centered on forward osmosis (FO) to extract high-quality water from real brackish groundwater and wastewater. The groundwater had salinity of 4g/L, while the wastewater sample consisted of a secondary effluent. These feed solutions were treated first in a FO step, achieving a recovery of 60%. Subsequently, the diluted draw solutions were subject to a nanofiltration (NF) step to regenerate their original osmotic pressure and to simultaneously collect a final permeate product. Magnesium chloride and sodium sulfate were both suitable draw solutes for this application. MgCl2 had a larger specific reverse salt flux and induced a more pronounced fouling-related flux decline with groundwater samples. Na2SO4 was re-concentrated with a higher permeability NF membrane but may require the use of anti-scalants. The average fluxes obtained in high-recovery batch FO were between 5 and 11 L m(-2)h(-1) with an initial bulk draw osmotic pressure in the range of 12-15 bar. Relatively low flux decline was observed in fouling experiments with both samples, while physical cleaning proved promising to recover the related loss in productivity. The final product waters were all of very high quality, suggesting the potential of this coupled system for water reuse and desalination. Some challenges related to the relatively low water flux in the FO step, as well as the loss of draw solutes and the gradual change in composition of the draw solution, need further analysis to establish the technical and economic feasibility of the system. (C) 2019 The Authors. Published by Elsevier Ltd.
机译:这项研究评估了一种以正渗透(FO)为中心的处理系统,该系统可从真正的咸淡地下水和废水中提取高质量的水。地下水的盐度为4g / L,而废水样品由次要废水组成。首先在FO步骤中处理这些进料溶液,回收率> 60%。随后,将稀释的汲取溶液进行纳滤(NF)步骤,以再生其原始渗透压并同时收集最终的渗透产物。氯化镁和硫酸钠都是适用于该应用的溶质。 MgCl2具有更大的比盐反比通量,并引起地下水样品污垢相关通量的下降。 Na2SO4用更高渗透率的NF膜重新浓缩,但可能需要使用防垢剂。高回收批次FO中获得的平均通量在5到11 L m(-2)h(-1)之间,初始大量抽吸渗透压在12-15 bar范围内。在两个样品的结垢实验中均观察到相对较低的通量下降,而物理清洁证明有望恢复相关的生产率损失。最终产品的水质都很高,这表明该耦合系统在回用水和脱盐方面具有潜力。与FO步骤中相对较低的水通量有关的一些挑战,以及牵引溶质的损失和牵引溶液组成的逐渐变化,需要进一步分析以建立该系统的技术和经济可行性。 (C)2019作者。由Elsevier Ltd.发布

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