High-flux TFN nanofiltration membranes incorporated with Camphor-Al2O3 nanoparticles for brackish water desalination

Chemosphere ◽  
2021 ◽  
Vol 265 ◽  
pp. 128999
Author(s):  
Yousra H. Kotp
2013 ◽  
Vol 425-426 ◽  
pp. 1-10 ◽  
Author(s):  
Lin Zhao ◽  
Philip C.-Y. Chang ◽  
Chi Yen ◽  
W.S.Winston Ho

2015 ◽  
Vol 476 ◽  
pp. 373-383 ◽  
Author(s):  
Hang Dong ◽  
Lin Zhao ◽  
Lin Zhang ◽  
Huanlin Chen ◽  
Congjie Gao ◽  
...  

2017 ◽  
Vol 5 (31) ◽  
pp. 16289-16295 ◽  
Author(s):  
Jing-Jing Wang ◽  
Hao-Cheng Yang ◽  
Ming-Bang Wu ◽  
Xi Zhang ◽  
Zhi-Kang Xu

Nanofiltration membranes are of great interest in brackish water desalination and drinking water purification.


Desalination ◽  
2004 ◽  
Vol 167 ◽  
pp. 403-409 ◽  
Author(s):  
Randa Haddada ◽  
Ezzedine Ferjani ◽  
Mohamed Sadok Roudesli ◽  
André Deratani

2011 ◽  
Vol 233-235 ◽  
pp. 2356-2358
Author(s):  
A A. Abuhabib ◽  
Abdul Wahab Mohammad ◽  
Rakmi Abd-Rahman

Nanofiltration membranes have proven their applicability in desalination as well as many other fields in water and wastewater industries. Two commercial nanofiltration membranes denoted as NF and ASP30 were chosen to be investigated in terms of their characteristics and performance in order to determine their suitability and applicability for brackish water desalination in Gaza Strip. In this work, membranes flux and rejection of two additional salts (Na2SO4 and KCl) is reported. Both membranes showed higher rejection rate for Na2SO4 (99% for NF and 75% for ASP30) when compared to KCl (36% for NF and 32% for ASP30). ASP30 had higher flux for both salts solutions (110 L.mˉ².hˉ¹ for Na2SO4 and 121 L.mˉ².hˉ¹ for KCl) while NF membrane had lower flux for both of them (78.4 L.mˉ².hˉ¹ for Na2SO4 and 72.5 L.mˉ².hˉ¹ for KCl). In addition, the variation of salt rejection versus permeation provides a possibility of optimizing operational conditions of both membranes. The results indicated good potential in applying both membranes to desalinate brackish water of Gaza Strip which is characterized by up to 2000 mg/l TDS of which Chloride is up to 700 mg/l.


2017 ◽  
Vol 83 ◽  
pp. 288-293
Author(s):  
A. Lhassani ◽  
H. Dach ◽  
Y.A. Boussouga

2020 ◽  
Author(s):  
Eyal Wormser ◽  
Oded Nir ◽  
Eran Edri

<div> <div> <div> <p>The desalination of brackish water provides water to tens of millions of people around the world, but current technologies deplete much needed nutrients from the water, which is detrimental to both public health and agriculture. A selective method for brackish water desalination, which retains the needed nutrients, is electrodialysis (ED) using monovalent-selective cation exchange membranes (MVS-CEMs). However, due to the trade-off between membrane selectivity and resistance, most MVS-CEMs demonstrate either high transport resistance or low selectivity, which increase energy consumption and hinder the use of such membranes for brackish water desalination by ED. Here, we used molecular layer deposition (MLD) to uniformly coat CEMs with ultrathin layers of alucone. The positive surface charge of the alucone instills monovalent selectivity in the CEM. Using MLD enabled us to precisely control and minimize the selective layer thickness, while the flexibility and nanoporosity of the alucone prevent cracking and delamination. Under conditions simulating brackish water desalination, this compound provides monovalent selectivity with negligible added resistance—the smallest reported resistance for a monovalent-selective layer, to date—thereby alleviating the selectivity–resistance trade-off. Addressing the water–energy nexus, we show that using these membranes in ED will cut at least half of the energy required for selective brackish water desalination with current MVS-CEMs. </p> </div> </div> </div>


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