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Received December 27, 2005
Accepted June 8, 2006
- This is an Open-Access article distributed under the terms of the Creative Commons Attribution Non-Commercial License (http://creativecommons.org/licenses/bync/3.0) which permits unrestricted non-commercial use, distribution, and reproduction in any medium, provided the original work is properly cited.
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Rejection of endocrine disrupters contained in biologically treated sewage by nanofiltration
Ulsan Regional Innovation Agency, #758-2 Yenamdong, Buggu, Ulsan 683-804, Korea 1Busan Environmental Technology Center, #216 Daeyeondong, Namgu, Busan 608-737, Korea
shijun55@utp.or.kr
Korean Journal of Chemical Engineering, September 2006, 23(5), 747-752(6), 10.1007/BF02705922
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Abstract
Two commercial nanofiltration membranes, NF-1 (low salt rejection) and NF-3 (medium salt rejection), were used for basic experiments on the rejection of endocrine disrupters of 17βestradiol, p-nonylphenol, bisphenol A and their mixed solution. Nanofiltration membrane experiments were carried out under low trans-membrane pressure of 0.5MPa as the operating condition. For the two nanofiltration membranes, the rejection factor was high when the pH of each feed solution was not adjusted. Based on the results of the nanofiltration membrane experiments, four commercial nanofiltration membranes--NF-1, NF-2 (medium salt rejection), NF-3 and NF-4 (high salt rejection)--were used for the rejection of endocrine disrupters contained in biologically treated sewage. The biologically treated sewage concentration of 0.039-0.055 μg/L as 17βestradiol equivalent was reduced by each nanofiltration membrane to 0.026 μg/ L (NF-1), 0.025 μg/L (NF-2), 0.003 μg/L (NF-3) and 0.009 μg/L (NF-4), as 17βestradiol equivalent, respectively. The rejection efficiency of endocrine disrupters showed the same tendency as the TOC rejection efficiency. The permeate flux of nanofiltration membranes was high in the order of NF-1, NF-3, NF-2 and NF-4.
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References
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