Effect of operating conditions and solution chemistry on model parameters in crossflow reverse osmosis of natural organic matter

Desalination ◽  
2010 ◽  
Vol 253 (1-3) ◽  
pp. 38-45 ◽  
Author(s):  
Supatpong Mattaraj ◽  
Wongphaka Phimpha ◽  
Pakasit Hongthong ◽  
Ratana Jiraratananon
Author(s):  
Börte Köse-Mutlu

Abstract In the current study, the effect of operating conditions including membrane characteristics and applied pressure on natural organic matter and sulphate removal of nanofiltration membranes for drinking water production was investigated. Water stress has been increasing all over the world due to population growth, climate change, and pollution; rainwater management stands out as one of the key solutions to this problem. Nanofiltration to treat rainwater stored in a cistern was studied. The objectives were sufficient treatment performance to overcome the taste problem and lower energy consumption. In this regard, three commercial nanofiltration membranes (NP010, NP030, and NF90) were used for the experiments carried out at 6–12 bar operating pressure regarding the response surface methodology. The correlation among the results of experiments and the model parameters were also calculated for all steps. According to the results, the effect of membrane characteristics was more abundant than the effect of the operating pressure. Finally, over 99% of natural organic matter and sulphate were eliminated in the optimum conditions. The results showed that it is possible to obtain treated rainwater with desired qualities, in a non-continuous NF plant operated at the pressure of 6 bar to reuse the rainwater and achieve water sustainability.


2006 ◽  
Vol 40 (18) ◽  
pp. 3385-3392 ◽  
Author(s):  
J.F. Koprivnjak ◽  
E.M. Perdue ◽  
P.H. Pfromm

2011 ◽  
Vol 78 (2) ◽  
pp. 189-200 ◽  
Author(s):  
A.W. Zularisam ◽  
Anwar Ahmad ◽  
Mimi Sakinah ◽  
A.F. Ismail ◽  
T. Matsuura

2015 ◽  
Vol 32 (1) ◽  
pp. 38-44 ◽  
Author(s):  
Nelson W. Green ◽  
Daniel McInnis ◽  
Norbert Hertkorn ◽  
Patricia A. Maurice ◽  
E. Michael Perdue

2002 ◽  
Vol 36 (9) ◽  
pp. 2357-2371 ◽  
Author(s):  
Patricia A. Maurice ◽  
Michael J. Pullin ◽  
Stephen E. Cabaniss ◽  
Qunhui Zhou ◽  
Ksenija Namjesnik-Dejanovic ◽  
...  

2012 ◽  
Vol 46 (16) ◽  
pp. 5343-5354 ◽  
Author(s):  
Jonathan G. Pressman ◽  
Daniel L. McCurry ◽  
Shahid Parvez ◽  
Glenn E. Rice ◽  
Linda K. Teuschler ◽  
...  

2016 ◽  
Vol 51 (2) ◽  
pp. 153-166
Author(s):  
Oswaldo Cerón Alfaro ◽  
Alejandra Martín Domínguez ◽  
Fotis Rigas ◽  
Myriam Solís-López ◽  
Rosa-María Ramírez-Zamora

We used an experimental design to determine the best coagulation–flocculation mechanism and the optimal operating conditions for the maximum removal of the natural organic matter fractions (hydrophobic acid (HPOA) and hydrophilic neutral (HPIN)), which are the main factors responsible for irreversible membrane fouling and the generation of disinfection by-products (DBPs). Charge neutralization and sweep mechanisms (SM) were studied using the jar test experiment, and synthetic waters prepared with different hydrophobic/hydrophilic (HPO/HPI) weight ratios by adding model compounds to represent the dissolved organic matter (DOM) fractions. Significant influence factors were identified for both coagulation mechanisms. The SM was the best one for DOM removal independent of the HPO/HPI weight ratio. The SM removed HPOA and HPIN fractions with efficiencies of 87.5–90.5% and 73.6–89.8%, respectively. The dissolved organic carbon (DOC) values of all met the recommendation proposed by the United States Environmental Protection Agency (2 mg total organic carbon (TOC)/L or 1.8 mg DOC/L) for DBPs (<100 μg/L). Furthermore, all effluents met the DOC and silt density index recommended values by membrane suppliers (<3 mg DOC/L and <5%/min, respectively) to minimize fouling potential and to extend the membrane life.


2006 ◽  
Vol 25 (S1) ◽  
pp. 268-268
Author(s):  
Jean F. Koprivnjak ◽  
E. Michael Perdue ◽  
Peter H. Pfromm

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