Removal Of Residual Organics From Drinking Water By Ozonation And Activated Carbon Filtration: A Pilot Plant Study

1995 ◽  
Vol 17 (4) ◽  
pp. 449-462 ◽  
Author(s):  
T.K. Kainulainen ◽  
T.A. Tuhkanen ◽  
T.K. Vartiainen ◽  
P.J. Kalliokoski
1988 ◽  
Vol 20 (8-9) ◽  
pp. 275-281 ◽  
Author(s):  
K. Terashima

The reduction of the musty odor substances 2-methylisoborneo1 (MIB) and geosmin, was investigated using a 60m3/day scale pilot plant. The ozone dose rate of 2-5mg/l was sufficient for the reduction of MIB and geosmin, and their reduction rates were between 75-100%. Two rapid sand filtrates, one pre-chlorinated and the other not pre-chlorinated,were introduced to the granular activated carbon (GAC) filters. Depending on which influent was used, the reduction rates were different and the GAC filter which filtered the water without pre-chlorination maintained its effectiveness in removing MIB and geosmin longer than the other. On the basis of these results, a 2000m3/day scale demonstration plant was constructed. The results of 1 year operation demonstrated the effectiveness of the method in removing musty odor substances from a large city water supply.


2002 ◽  
Vol 2 (1) ◽  
pp. 139-146 ◽  
Author(s):  
P.A.C. Bonné ◽  
J.A.M.H. Hofman ◽  
J.P. van der Hoek

Since March 1995 Amsterdam Water Supply has applied biological activated carbon filtration (BACF) in the treatment process of the Leiduin plant. In this plant (capacity 70 × 106 m3/y) pretreated River Rhine water is infiltrated in the dune area, west of Amsterdam, for artificial recharge. Post treatment comprises rapid sand filtration, ozonation, hardness removal, biological activated carbon filtration and slow sand filtration. At the start the carbon reactivation frequency was set at 18 months, based on removal efficiencies for AOX (adsorbable organic halogens), DOC, pesticides and micropollutants. After four years of operation of a pilot plant (10 m3/hour) in parallel with the full-scale plant, the remaining removal capacity and the break-through profile of the carbon filters was investigated. In contrast to the full-scale plant, no carbon reactivation was applied in the pilot plant during the operation of 4 years. Spiking experiments were carried out after ozonation, in the influent of the biological activated carbon filtration with a cocktail of different pesticides after 1.5, 3 and 4 years. Influent concentrations varied between 2 to 10 μg/l. Without carbon reactivation the filter effluent still complies with the Dutch drinking water standards and guide lines, as well as with the Amsterdam Water Supply standards: DOC is less than 2 mg/l (actually 1.2 mg/l) and AOX remains below 5 μg/l. After four years, with spiking concentrations of 2 μg/l still no pesticide break-through was observed in the two-stage biological activated carbon filtration process. It can be concluded that a running time of 3 years between two reactivations in the two stage biological active carbon filtration is achievable, without negatively affecting the finished water quality. Average DOC concentrations will increase up to 1.2 mg/l, from 1 mg/l with running times of 2 years. After four years or 100,000 bedvolumes the AOC content is equal to or lower than 10 μg/l after biological activated carbon filtration. With slow sand filtration at the end and as polishing step AOC will be less than 10-5 μg/l. With every extension of six months duration time a saving of Euro 305,000 on reactivation costs is possible. With every 6 month extension of the running time of the carbon filters a saving of €610,000 is realised on the reactivation costs of the Leiduin treatment plant.


2013 ◽  
Vol 13 (1) ◽  
pp. 74-88
Author(s):  
Juan Carlos García Prieto ◽  
Patricia Pérez Galende ◽  
Juan Manuel Cachaza Silverio ◽  
Manuel García Roig

This study reports a procedure for the evaluation and comparison of the adsorption and filtration capacities of commercial activated carbons in the treatment of drinking water and the design and operation of a pilot plant to simulate the behavior of fast open filters made of granular activated carbon. The milestone of this experimental work was to determine the adsorption and filtration capacities and the physicochemical properties of five commercial activated carbons with a view to determining which activated carbon might replace the open sand filters of the drinking water treatment plant (DWTP) of the city of Salamanca (western Spain). Compliance with the requirements and physicochemical characteristics stipulated in the EN 12915 European standard for the different activated carbons tested was analyzed, and studies of the prewashing and behavior of the carbons operating in the filters were performed. In this sense, filtration tests to study the saturation of the bed, the variations in pressure drop and the performance of the removal of organic matter in suspension were carried out. Furthermore, the optimal time and rate of the countercurrent washing of the filters and the expansion of the filter bed were evaluated. In the adsorption assays, the specific surface area, porosity, useful lifetime and capacity of adsorption of the dissolved organic matter –especially humic acids, the major precursors of water chlorination by-products – of the activated carbons were determined. The results not only provided an overview of the actual behavior of different types of commercial activated carbons from their initial installation up to the end of their useful life, but also permitted optimization of the filtration and adsorption processes that could lead to the corresponding economic savings and energy reduction in the use of such activated carbon filter-adsorbers.


1984 ◽  
Vol 6 (2) ◽  
pp. 71-86 ◽  
Author(s):  
Wayne F. Lorenz ◽  
K. Daniel Linstedt ◽  
Edwin R. Bennett

2016 ◽  
Vol 94 (7) ◽  
pp. 1277-1284 ◽  
Author(s):  
Tássia Rhuna Tonial dos Santos ◽  
Milene Carvalho Bongiovani ◽  
Marcela Fernandes Silva ◽  
Letícia Nishi ◽  
Priscila Ferri Coldebella ◽  
...  

Chemosphere ◽  
2013 ◽  
Vol 92 (2) ◽  
pp. 184-191 ◽  
Author(s):  
Eliane Sloboda Rigobello ◽  
Angela Di Bernardo Dantas ◽  
Luiz Di Bernardo ◽  
Eny Maria Vieira

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