Removal of natural organic matter by ion exchange: Comparing regenerated and non-regenerated columns

2021 ◽  
Vol 189 ◽  
pp. 116661 ◽  
Author(s):  
Michael Edgar ◽  
Treavor H. Boyer
2018 ◽  
Vol 146 ◽  
pp. 1-9 ◽  
Author(s):  
Nargess Amini ◽  
Isabelle Papineau ◽  
Veronika Storck ◽  
Pierre R. Bérubé ◽  
Madjid Mohseni ◽  
...  

2002 ◽  
Vol 2 (5-6) ◽  
pp. 445-450 ◽  
Author(s):  
D.H. Kim ◽  
S.-H. Moon ◽  
J. Cho

A series of adsorption experiments were performed to investigate the factors affecting the transport of natural organic matter (NOM) in an ion-exchange (IX) membrane. In this study, the structure of the NOM was hypothesized to be an important factor in terms of the organic fouling of IX membrane. It was found that the adsorbed mass of hydrophobic NOM constituent on the membrane surface was higher than that of either the hydrophilic or transphilic NOM constituent. NOM adsorption was seriously affected by the apparent charge of the NOM. As the apparent charge increased, NOM adsorption also significantly increased. Moreover, the molecular mass of the hydrophobic NOM acids was too high to enable them to pass through the IX membrane, and this caused an accumulated adsorption of solutes on the membrane surface, i.e. NOM fouling. In addition, both pH and ionic strength affected NOM adsorption on the surface of the IX membrane. Lower NOM adsorption resulted from a lower pH and a higher ionic strength.


1999 ◽  
Vol 40 (9) ◽  
pp. 183-190 ◽  
Author(s):  
S. G. J. Heijman ◽  
A. M. van Paassen ◽  
W. G. J. van der Meer ◽  
R. Hopman

For the removal of DOC (and colour) several treatment steps are suggested. If it is also necessary to remove hardness nanofiltration is probably the first choice. For colour removal without softening a number of adsorbents are suggested in the literature. In order to estimate the costs of these treatment steps a dynamic column model based on batch experiments was used to predict the service time of the columns filled with different adsorbents. Also the (on site) regeneration of the different adsorbents was investigated in batch experiments. Especially the ion exchange resin was very promising. The costs of the treatment of one m3 water with a column filled with an ion exchange resin was estimated for the investigated case at 0.05 Euro.


2018 ◽  
Vol 146 ◽  
pp. 256-263 ◽  
Author(s):  
P. Finkbeiner ◽  
J. Redman ◽  
V. Patriarca ◽  
G. Moore ◽  
B. Jefferson ◽  
...  

Sign in / Sign up

Export Citation Format

Share Document