Biological Filtration for Ozone and Chlorine DBP Removal |
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Authors: | Paul Wobma David Pernitsky Bill Bellamy Kelly Kjartanson Keith Sears |
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Affiliation: | 1. CH2M Gore &2. Storrie Ltd. , 1500,555 4th Avenue S.W. Calgary, AB, T2P 3E7;3. CH2M HILL Engineering Ltd. , 1500,555 4th Avenue S.W. Calgary, AB, T2P 3E7;4. City of Winnipeg, Manitoba , 1500,555 4th Avenue S.W., Calgary, AB, T2P 3E7;5. Reid Crowther &6. Partners Ltd , 1500,555 4th Avenue S.W. Calgary, AB, T2P 3E7 |
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Abstract: | This paper presents results from a water treatment pilot testing program in Winnipeg, Canada (pop. 650,000) which evaluated a DAF/ozone/deep bed filtration process. As part of the testing program, biological filtration using GAC and anthracite media was assessed for the removal of ozone DBPs and background chlorine DBPs (due to upstream chlorination of the source water). The results were used to evaluate the effectiveness of biological filtration for DBP removal. High filtration rates were tested in this study. The 2.1m deep filters were run at a hydraulic loading rate (HLR) of 35 m/h with an empty bed contact time (EBCT) of only 3.6 minutes. The important findings of this work are ?The high-rate biologically active carbon (BAC) filters met the objective of controlling ozone DBPs. These results confirm that high rate, low EBCT filters can provide significant biodegradation. Anthracite biofilters provided significantly less removal of ozone DBPs. ?The high rate BAC filters showed significant reduction of background HAAs. BAC reduced the background HAAs to below the long-term target of 30 μg/L. Anthracite biofilters did not exhibit HAA removal. ?Biological filtration with either media was ineffective for background THM removal. The long-term target of 40 μg/L could not be achieved without GAC adsorption. |
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Keywords: | Ozone Disinfection By-Products Granular Activated Carbon Biological Activated Carbon Aldehydes Carboxylic Acids Keto Acids Trihalomethanes Haloacetic Acids |
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