The discharge of nitrogen in wastewater treatment plant effluent has been identified as a receiving water quality issue throughout the United States and in the European Community. Regulatory agencies are evaluating discharge limits for total nitrogen (TN) as low as 3 to 5 mg/l. To attain these limits at treatment plants with little or no space for expansion, technologies which can remove large quantities of nitrogen with relatively small space requirements are required. Biological upflow fluidized bed (BFB) technology appears to be well suited to these regions. This paper describes the results of a demonstration project using a fluidized bed reactor. The reactor was operated at a flow rate of 15 l/s and an average daily loading of 1843 kg NO3/1000 m3/d and maximum loadings of 6407 kg NO3/1000 m3/d. At steady-state conditions, effluent total nitrogen concentrations averaged 2.5 mg/l over a temperature range of 11 to 25°C. At high nitrate loading rates, effluent total nitrogen concentrations averaged 4.1 mg/l. Approximately 3 mg of methanol per mg of influent nitrate was used as a carbon source. Reactor empty bed contact time averaged 5.7 minutes.
Biological upflow fluidized bed denitrification reactor demonstration project - Stamford, CT, USA
Jeannette Semon, Thomas Sadick, Dennis Palumbo, Marylee Santoro, Peter Keenan; Biological upflow fluidized bed denitrification reactor demonstration project - Stamford, CT, USA. Water Sci Technol 1 July 1997; 36 (1): 139–146. doi: https://doi.org/10.2166/wst.1997.0032
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