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使用疏水和亲水涂层聚四氟乙烯(PTFE)膜对含表面活性剂纺织废水进行膜蒸馏试验

Membrane Distillation Trial on Textile Wastewater Containing Surfactants Using Hydrophobic and Hydrophilic-Coated Polytetrafluoroethylene (PTFE) Membranes.

作者信息

Villalobos García Jesús, Dow Noel, Milne Nicholas, Zhang Jianhua, Naidoo Leslie, Gray Stephen, Duke Mikel

机构信息

Institute for Sustainable Industries & Liveable Cities, Victoria University, P.O. Box 14428, Melbourne, VIC 8001, Australia.

Australian Textile Mills Pty Ltd., Wangaratta, VIC 3677, Australia.

出版信息

Membranes (Basel). 2018 Jun 15;8(2):31. doi: 10.3390/membranes8020031.

DOI:10.3390/membranes8020031
PMID:29914072
原文链接:https://pmc.ncbi.nlm.nih.gov/articles/PMC6027291/
Abstract

Treating wastewater from textile plants using membrane distillation (MD) has great potential due to the high-salinity wastes and availability of waste heat. However, textile wastewaters also contain surfactants, which compromise the essential hydrophobic feature of the membrane, causing membrane wetting. To address this wetting issue, a custom-made membrane consisting of a hydrophilic layer coated on hydrophobic polytetrafluoroethylene (PTFE) was tested on textile wastewater in a pilot MD setup, and compared with a conventional hydrophobic PTFE membrane. The test was carried out with a feed temperature of 60 °C, and a permeate temperature of 45 °C. The overall salt rejection of both membranes was very high, at 99%. However, the hydrophobic membrane showed rising permeate electrical conductivity, which was attributed to wetting of the membrane. Meanwhile, the hydrophilic-coated membrane showed continually declining electrical conductivity demonstrating an intact membrane that resisted wetting from the surfactants. Despite this positive result, the coated membrane did not survive a simple sodium hydroxide clean, which would be typically applied to a membrane process. This brief study showed the viability of membrane distillation membranes on real textile wastewaters containing surfactants using hydrophilic-coated hydrophobic PTFE, but the cleaning process required for membranes needs optimization.

摘要

由于纺织厂废水盐度高且有废热可用,采用膜蒸馏(MD)处理纺织厂废水具有巨大潜力。然而,纺织废水还含有表面活性剂,这会损害膜的基本疏水特性,导致膜湿润。为解决这一湿润问题,在中试MD装置中,对一种由涂覆在疏水性聚四氟乙烯(PTFE)上的亲水层组成的定制膜进行了纺织废水测试,并与传统的疏水性PTFE膜进行了比较。测试在进料温度为60℃、渗透液温度为45℃的条件下进行。两种膜的总脱盐率都非常高,达到99%。然而,疏水膜的渗透液电导率不断上升,这归因于膜的湿润。同时,亲水涂层膜的电导率持续下降这表明膜完好无损,能够抵抗表面活性剂的湿润。尽管取得了这一积极成果,但涂覆膜在通常用于膜工艺的简单氢氧化钠清洗中未能幸存下来。这项简短的研究表明,使用亲水涂层疏水性PTFE的膜蒸馏膜处理含表面活性剂的实际纺织废水是可行的,但膜所需的清洗过程需要优化。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/8123b2c4b68d/membranes-08-00031-g010.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/853404408e56/membranes-08-00031-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/d33b7443530d/membranes-08-00031-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/8a1caf06f612/membranes-08-00031-g003.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/e50d2a3d0cc1/membranes-08-00031-g004.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/6283e4122b70/membranes-08-00031-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/9889e1172ebd/membranes-08-00031-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/e8a76b0742eb/membranes-08-00031-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/72038f69ec17/membranes-08-00031-g008.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/185c032089aa/membranes-08-00031-g009.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/8123b2c4b68d/membranes-08-00031-g010.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/853404408e56/membranes-08-00031-g001.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/d33b7443530d/membranes-08-00031-g002.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/8a1caf06f612/membranes-08-00031-g003.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/e50d2a3d0cc1/membranes-08-00031-g004.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/6283e4122b70/membranes-08-00031-g005.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/9889e1172ebd/membranes-08-00031-g006.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/e8a76b0742eb/membranes-08-00031-g007.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/72038f69ec17/membranes-08-00031-g008.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/185c032089aa/membranes-08-00031-g009.jpg
https://cdn.ncbi.nlm.nih.gov/pmc/blobs/9e87/6027291/8123b2c4b68d/membranes-08-00031-g010.jpg

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