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阻垢剂在提高处理厌氧地下水的反渗透系统回收率中的污垢物鉴定及性能评估

Foulant Identification and Performance Evaluation of Antiscalants in Increasing the Recovery of a Reverse Osmosis System Treating Anaerobic Groundwater.

作者信息

Mangal Muhammad Nasir, Salinas-Rodriguez Sergio G, Dusseldorp Jos, Blankert Bastiaan, Yangali-Quintanilla Victor A, Kemperman Antoine J B, Schippers Jan C, van der Meer Walter G J, Kennedy Maria D

机构信息

IHE Delft Institute for Water Education, Water Supply, Sanitation and Environmental Engineering Department, Westvest 7, 2611 AX Delft, The Netherlands.

Faculty of Science and Technology, University of Twente, 7500 AE Enschede, The Netherlands.

出版信息

Membranes (Basel). 2022 Mar 2;12(3):290. doi: 10.3390/membranes12030290.

DOI:10.3390/membranes12030290
PMID:35323764
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC8950045/
Abstract

The objectives of this study are to assess the performance of antiscalants in increasing the recovery (≥85%) of a reverse osmosis (RO) plant treating anaerobic groundwater (GW) in Kamerik (the Netherlands), and to identify scalants/foulant that may limit RO recovery. Five different commercially available antiscalants were compared on the basis of their manufacturer-recommended dose. Their ability to increase the recovery from 80% to a target of 85% was evaluated in pilot-scale measurements with anaerobic GW and in once-through lab-scale RO tests with synthetic (artificial) feedwater. A membrane autopsy was performed on the tail element(s) with decreased permeability. X-ray photoelectron spectroscopy (XPS) analysis indicated that calcium phosphate was the primary scalant causing permeability decline at 85% recovery and limiting RO recovery. The addition of antiscalant had no positive effect on RO operation and scaling prevention, since at 85% recovery, permeability of the last stage decreased with all five antiscalants, while no decrease in permeability was observed without the addition of antiscalant at 80% recovery. In addition, in lab-scale RO tests executed with synthetic feed water containing identical calcium and phosphate concentrations as the anaerobic GW, calcium phosphate scaling occurred both with and without antiscalant at 85% recovery, while at 80% recovery without antiscalant, calcium phosphate did not precipitate in the RO element. In brief, calcium phosphate appeared to be the main scalant limiting RO recovery, and antiscalants were unable to prevent calcium phosphate scaling or to achieve a recovery of 85% or higher.

摘要

本研究的目的是评估阻垢剂在提高荷兰卡默里克处理厌氧地下水(GW)的反渗透(RO)装置回收率(≥85%)方面的性能,并识别可能限制RO回收率的结垢剂/污染物。根据制造商推荐的剂量,对五种不同的市售阻垢剂进行了比较。在中试规模下用厌氧GW进行测量,并在实验室规模下用合成(人工)给水进行单通道RO测试,评估它们将回收率从80%提高到目标85%的能力。对渗透率降低的尾端元件进行了膜解剖。X射线光电子能谱(XPS)分析表明,磷酸钙是导致在85%回收率下渗透率下降并限制RO回收率的主要结垢剂。添加阻垢剂对RO运行和防垢没有积极影响,因为在85%回收率下,使用所有五种阻垢剂时最后阶段的渗透率都会降低,而在80%回收率下不添加阻垢剂时未观察到渗透率下降。此外,在实验室规模的RO测试中,使用含有与厌氧GW相同钙和磷浓度的合成给水,在85%回收率下添加和不添加阻垢剂时都会发生磷酸钙结垢,而在80%回收率下不添加阻垢剂时,RO元件中不会析出磷酸钙。简而言之,磷酸钙似乎是限制RO回收率的主要结垢剂,阻垢剂无法防止磷酸钙结垢或实现85%或更高的回收率。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/e4fe57847220/membranes-12-00290-g010.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/dfb45b51b101/membranes-12-00290-g001.jpg
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https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/665a51d29f3b/membranes-12-00290-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/06d192b63ba2/membranes-12-00290-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/0f2e8bfcf073/membranes-12-00290-g008.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/732b9d15cb78/membranes-12-00290-g009.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/e4fe57847220/membranes-12-00290-g010.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/dfb45b51b101/membranes-12-00290-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/2558948b8667/membranes-12-00290-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/baafd58b427d/membranes-12-00290-g003.jpg
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https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/5a63573e2a6c/membranes-12-00290-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/665a51d29f3b/membranes-12-00290-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/06d192b63ba2/membranes-12-00290-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/0f2e8bfcf073/membranes-12-00290-g008.jpg
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https://cdn.ncbi.nlm.nih.gov/pmc/blobs/a9ac/8950045/e4fe57847220/membranes-12-00290-g010.jpg

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