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采用正向渗透与纳滤耦合淡化地下咸水和再利用废水回收汲取液。

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

机构信息

Department of Environment, Land and Infrastructure Engineering (DIATI), Politecnico di Torino, Corso Duca degli Abruzzi 24, 10129, Turin, Italy.

Department of Environment, Land and Infrastructure Engineering (DIATI), Politecnico di Torino, Corso Duca degli Abruzzi 24, 10129, Turin, Italy; CleanWaterCenter@PoliTo, Politecnico di Torino, Corso Duca degli Abruzzi 24, 10129, Turin, Italy.

出版信息

Water Res. 2019 Apr 15;153:134-143. doi: 10.1016/j.watres.2019.01.014. Epub 2019 Jan 22.

DOI:10.1016/j.watres.2019.01.014
PMID:30708192
Abstract

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 4 g/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. MgCl had a larger specific reverse salt flux and induced a more pronounced fouling-related flux decline with groundwater samples. NaSO 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 mh 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.

摘要

本研究评估了一种以正向渗透(FO)为核心的处理系统,用于从真实的微咸地下水和废水提取高质量的水。地下水的盐度为 4g/L,而废水样本由二级出水组成。这些进料溶液首先在 FO 步骤中进行处理,实现了超过 60%的回收率。随后,稀释的汲取液经过纳滤(NF)步骤再生其原始渗透压,并同时收集最终的渗透产物。氯化镁和硫酸钠都是该应用的合适汲取剂。MgCl 的反向盐通量更大,并且在用地下水样本时会导致更明显的与污染相关的通量下降。NaSO 可以用具有更高渗透性的 NF 膜再浓缩,但可能需要使用防垢剂。在高回收率批量 FO 中获得的平均通量在 5 到 11L/mh 之间,初始总汲取渗透压在 12-15bar 范围内。在两个样本的污染实验中观察到的通量下降相对较低,而物理清洗证明可以恢复相关的生产力损失。最终的产水水质都非常高,表明该耦合系统在水再利用和脱盐方面具有潜力。FO 步骤中通量相对较低、汲取剂损失以及汲取液组成逐渐变化等相关挑战需要进一步分析,以确定该系统的技术和经济可行性。

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