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Nitrate removal from three different effluents using large-scale denitrification beds
Authors:L.A. Schipper  S.C. Cameron  S. Warneke
Affiliation:1. Department of Earth and Ocean Sciences, University of Waikato, Private Bag 3105, Hamilton, New Zealand;2. GNS Science, Taupo, New Zealand;1. University of Waikato, Private Bag 3105, Hamilton, New Zealand;2. NIWA, National Institute of Water and Atmospheric Research, P.O. Box 11115, Hamilton, New Zealand;1. Iowa Geological Survey, Trowbridge Hall, University of Iowa, Iowa City, IA, United States;2. Iowa Soybean Association, Ankeny, IA, United States;3. The Nature Conservancy, Des Moines, IA, United States;1. School of Biological Sciences, University of Canterbury, Private Bag 4800, Christchurch 8140, New Zealand;2. Institute of Environmental Science and Research, Environmental Science Centre, 27 Creyke Road, Christchurch 8540, New Zealand;3. School of Environment, University of Auckland, Science Centre 302, 23 Symonds Street, Auckland 1010, New Zealand;1. 111 Wing Drive, Biological & Environmental Engineering, Cornell University, Ithaca, NY, 14853, USA;2. 111 Wing Drive, Cornell University, Ithaca, NY, 14853, USA
Abstract:Simple technologies that remove nitrate from effluents and other point discharges need to be developed to reduce pollution of receiving waters. Denitrification beds are lined containers filled with organic carbon (typically wood chip or coarse sawdust) and are a technology that is proving promising. Water containing NO3? (treated effluent or agricultural drainage) is passed through the bed and the wood chips act as an energy source for denitrifying bacteria that convert NO3? to N gases. There are few data on the efficiency of NO3 removal in large-scale beds. We report here NO3? removal results from three large denitrification beds with volumes of 83, 294, and 1320 m3 treating dairy shed effluent, treated domestic effluent and glasshouse effluent, respectively. Nitrate was nearly completely removed from the dairy shed effluent (annual load of 31 kg N) and domestic effluent (annual load 365 kg N). In these beds, NO3? removal, presumably by denitrification, was limited by NO3? concentration. However, the bed treating glasshouse effluent was overwhelmed by very high NO3? concentration (about 250 g N m?3) and high flow rates (about 150 m3 d?1) but still reduced NO3? concentration to about 150 g N m?3. For this bed, long-term NO3? removal was between 5 and 10 g N m?3 of bed material when NO3? was non-limiting and was similar to rates reported for other smaller denitrification beds. As expected, organic N, ammonium and phosphorus were not removed from any of the effluents following passage through the beds. Our results suggest that denitrification beds are a relatively inexpensive system to construct and operate, and are suitable for final treatment of a range of NO3?-laden effluents.
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