Transformation of Trace Organic Contaminants from Reverse Osmosis Concentrate by Open-Water Unit-Process Wetlands with and without Ozone Pretreatment

2020 ◽  
Vol 54 (24) ◽  
pp. 16176-16185
Author(s):  
Rachel C. Scholes ◽  
Jacob F. King ◽  
William A. Mitch ◽  
David L. Sedlak
2014 ◽  
Vol 48 (9) ◽  
pp. 5136-5144 ◽  
Author(s):  
Justin T. Jasper ◽  
Zackary L. Jones ◽  
Jonathan O. Sharp ◽  
David L. Sedlak

2011 ◽  
Vol 45 (4) ◽  
pp. 1579-1586 ◽  
Author(s):  
Jelena Radjenovic ◽  
Arseto Bagastyo ◽  
René A. Rozendal ◽  
Yang Mu ◽  
Jürg Keller ◽  
...  

2012 ◽  
Vol 46 (8) ◽  
pp. 2683-2692 ◽  
Author(s):  
Ming Xie ◽  
Long D. Nghiem ◽  
William E. Price ◽  
Menachem Elimelech

2013 ◽  
Vol 30 (8) ◽  
pp. 421-436 ◽  
Author(s):  
Justin T. Jasper ◽  
Mi T. Nguyen ◽  
Zackary L. Jones ◽  
Niveen S. Ismail ◽  
David L. Sedlak ◽  
...  

Membranes ◽  
2021 ◽  
Vol 11 (1) ◽  
pp. 33
Author(s):  
Norbert Konradt ◽  
Jan Gerrit Kuhlen ◽  
Hans-Peter Rohns ◽  
Birgitt Schmitt ◽  
Uwe Fischer ◽  
...  

In response to increasingly stringent restrictions for drinking water quality, a parallel operation of two common technologies, low-pressure reverse osmosis (LPRO) and activated carbon filtration (ACF), was investigated in a comprehensive five-month pilot study for the removal of 32 typical trace organic contaminants (TrOCs) from Rhine bank filtrates employing a semi- technical plant. TrOCs have been divided into three groups: polyfluorinated aliphatic compounds; pharmaceuticals, pesticides and metabolites; in addition to volatiles, nitrosamines and aminopolycarboxylic acids, which were also examined. The net pressure behavior, normalized salt passage and rejection of TrOCs by LPRO were investigated and compared with ACF operation. In addition, autopsies from the leading and last membrane modules were performed using adenosine triphosphate (ATP), total organic carbon (TOC), ICP-OES and SEM-EDX techniques. Generally, rather stable LPRO membrane performance with limited membrane fouling was observed. TrOCs with a molecular weight of ≥ 150 Da were completely retained by LPRO, while the rejection of di- and trichloro compounds improved as the filtration progressed. ACF also showed significant removal for most of the TrOCs, but without desalination. Accordingly, the ACF and LPRO can be operated in parallel such that the LPRO permeate and the ACF-treated bypass can be mixed to produce drinking water with adjustable hardness and significantly reduced TrOCs.


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