scholarly journals Study of the Effect of Nanoparticles and Surface Morphology on Reverse Osmosis and Nanofiltration Membrane Productivity

Membranes ◽  
2013 ◽  
Vol 3 (3) ◽  
pp. 196-225 ◽  
Author(s):  
Yuming Fang ◽  
Steven Duranceau
Biofouling ◽  
2011 ◽  
Vol 27 (2) ◽  
pp. 173-183 ◽  
Author(s):  
Mohiuddin Md. Taimur Khan ◽  
Philip S. Stewart ◽  
David J. Moll ◽  
William E. Mickols ◽  
Sara E. Nelson ◽  
...  

Desalination ◽  
2001 ◽  
Vol 138 (1-3) ◽  
pp. 259-270 ◽  
Author(s):  
C.A.C. van de Lisdonk ◽  
B.M. Rietman ◽  
S.G.J. Heijman ◽  
G.R. Sterk ◽  
J.C. Schippers

2012 ◽  
Vol 441 ◽  
pp. 584-588
Author(s):  
San Chuan Yu ◽  
Zhi Wen Chen ◽  
Mei Hong Liu ◽  
Jing Wei Zhao

In view of the water shortage, the increasingly severe regulations as well as the release thresholds, it is becoming increasingly necessary to reuse the textile effluents. This work concerned the treatment of textile plant effluent after conventional biological processing by membrane technology for water reuse. Desal5 DK nanofiltration (NF) membrane and BW30 reverse osmosis (RO) membrane were investigated in this study in terms of COD and color removal, salinity reduction as well as permeate flux through cross-flow permeation tests. The results showed that the Desal5 DK nanofiltration membrane exhibited higher stabilized water permeability and flux decline than the reverse osmosis membrane because of its higher porosity and tendency towards fouling. The BW30 reverse osmosis membrane reduced salinity to a great extent than the Desal5 DK nanofiltration membrane. While the nanofiltration membrane exhibited better COD removal efficiency compared to the RO membrane, possibly due to its sieving removal mechanism. The treated water with good enough quality could be recycled back into the process, thereby offering economical benefits by reducing the water consumption and wastewater treatment cost.


2019 ◽  
Vol 97 ◽  
pp. 06004 ◽  
Author(s):  
Alexei Pervov ◽  
Xuan Quyet Nguyen

Main disadvantages of state of the art membrane techniques are discussed with respect to the problem of concentrate disposal. Possible ways to improve conventional membrane techniques and to radically decrease the number of effluents discharged are proposed. Application of newly developed “open channel” membrane modules that do not contain “dead” areas enables us to develop and implement into practice new techniques to reduce and even utilize concentrates of membrane units. Experiments demonstrated a possibility to reduce concentrate flow due to deposition of excessive calcium as calcium carbonate on seed crystals in the reactor. Flow diagrams for different cases of natural water composition are described and discussed that demonstrate newly developed techniques to produce drinking quality water using reverse osmosis and nanofiltration membrane facilities with high recoveries.


2020 ◽  
Vol 10 (5) ◽  
pp. 671-679
Author(s):  
Mahmoud Fathy ◽  
Abeer El Shahawy ◽  
Th. Abdel Moghny ◽  
Ayman Nafady

Treatment and cleaning of reverse osmosis (RO) membranes saturated with CaCO3/brine is a main issue in RO desalination processes. Herein, a Cu–ZnO-polyvinyl chloride (PVC)-nylon nanofiltration membrane was synthesized and utilized to minimize and/or eliminate CaCO3/brine during RO, along with probing the effects of Cu–ZnO antiscalant on calcite precipitation in normal aqueous and supersaturated CaCO3/brine solutions. Moreover, decreases in Ca2+ content over time were evaluated by electrical conductivity and pH measurements. Results revealed that Cu–ZnO nanocomposite substantially increases induction time and stimulates the formation of aragonite rather than calcite. A 2 mg/L dose of Cu–ZnO nanocomposite suppressed CaCO3 in both unsaturated and supersaturated solutions. In natural water sources (containing ∼500 mg/L calcium and ≈300 mg/L bicarbonate content), complete removal of CaCO3 blockage was achieved by using 2.5 mg/L of Cu–ZnO antiscalant, while in supersaturated water solutions (1000 mg/L calcium and ≈500 mg/L bicarbonate content), only 2 mg/L of Cu–ZnO antiscalant was required to fully remove the blockage. Importantly, addition of 2 mg/L of Cu–ZnO antiscalant to RO brine showed no apparent deposition on the membrane surface after 6 h, with a minimal flux decrease to 86.5%. Thus, Cu–ZnO-PVC-nylon nanofiltration membranes with low concentrations (2 mg/L) of Cu–ZnO antiscalant can play a significant role in the treatment of supersaturated CaCO3/brine water discharge.


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