Development of an attached growth reactor for NH 4 –N removal at a drinking water supply system in Kathmandu Valley, Nepal.

Higher concentrations of ammonium (NH4–N) and iron (Fe) than a standard for drinking are typical characteristics of groundwater in the study area. To remove NH4–N and Fe, the drinking water supply system in this study consists of a series of treatment units (i.e., aeration and sedimentation, filtration, and chlorination); however, NH4−N in treated water is higher than a standard for drinking (i.e., <1.5 mg NH4–N/L). The objective of this study, therefore, is to develop an attached growth system containing a fiber carrier for reducing NH4–N concentration within a safe level in the treated water. To avoid the need of air supply for nitrification, groundwater was continuously dripped through the reactor. It made the system simple operation and energy efficient. Effects of reactor design (reactor length and carrier area) were studied to achieve a high NH4−N removal efficiency. In accordance with raw groundwater characteristics in the area, effects of low inorganic carbon (IC) and phosphate (PO4–P) and high Fe on the removal efficiency were also investigated. The results showed a significant increase in NH4–N removal efficiency with reactor length and carrier area. A low IC and PO4–P had no effect on NH4–N removal, whereas a high Fe decreased the efficiency significantly. The first 550 days operation of a pilot−scale reactor installed in the drinking water supply system showed a gradual increase in the efficiency, reaching to 95−100%, and stability in the performance even with increased flow rate from 210 to 860 L/day. The high efficiency of the present work was indicated because only less than 1 mg of NH4−N/L was left over in the treated water. [ABSTRACT FROM AUTHOR]