scholarly journals Current and Long-Term Effects of Delta Water Quality on Drinking Water Treatment Costs from Disinfection Byproduct Formation

Author(s):  
Wei–Hsiang Chen ◽  
◽  
Kristine Haunschild ◽  
Jay R. Lund ◽  
William Fleenor ◽  
...  
2008 ◽  
Vol 8 (4) ◽  
pp. 363-375 ◽  
Author(s):  
S. Panglisch ◽  
W. Dautzenberg ◽  
A. Holy

In November 2005 one of the largest combined coagulation ultrafiltration plants worldwide and the largest in Germany went into operation. Its maximum capacity is about 7,000 m3/h of drinking water. Furthermore, a secondary UF stage with a capacity of about 630 m3/h has been used to treat the backwash water of the first stage. The innovative plant design results from an intensive preliminary pilot period, during which several advanced concepts were investigated. The paper reflects the long-term experience with operation and monitoring of the plant over a period of about two years. Up to now, expectations regarding performance in terms of permeability, retention, and reliability have been exceeded. The predicted specific treatment costs of about 10 €Ct/m3 drinking water were achieved or even reduced.


2013 ◽  
Vol 6 (1) ◽  
pp. 1-10 ◽  
Author(s):  
A. Grefte ◽  
M. Dignum ◽  
E. R. Cornelissen ◽  
L. C. Rietveld

Abstract. To guarantee a good water quality at the customers tap, natural organic matter (NOM) should be (partly) removed during drinking water treatment. The objective of this research was to improve the biological stability of the produced water by incorporating anion exchange (IEX) for NOM removal. Different placement positions of IEX in the treatment lane (IEX positioned before coagulation, before ozonation or after slow sand filtration) and two IEX configurations (MIEX® and fluidized IEX (FIX)) were compared on water quality as well as costs. For this purpose the pre-treatment plant at Loenderveen and production plant Weesperkarspel of Waternet were used as a case study. Both, MIEX® and FIX were able to remove NOM (mainly the HS fraction) to a high extent. NOM removal can be done efficiently before ozonation and after slow sand filtration. The biological stability, in terms of assimilable organic carbon, biofilm formation rate and dissolved organic carbon, was improved by incorporating IEX for NOM removal. The operational costs were assumed to be directly dependent of the NOM removal rate and determined the difference between the IEX positions. The total costs for IEX for the three positions were approximately equal (0.0631 € m−3), however the savings on following treatment processes caused a cost reduction for the IEX positions before coagulation and before ozonation compared to IEX positioned after slow sand filtration. IEX positioned before ozonation was most cost effective and improved the biological stability of the treated water.


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