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Nitrogen and Phosphorous Removal From Aerated Lagoon Effluent Using Horizontal Roughing Filter (Hrf) Publisher



Khazaei M1 ; Nabizadeh R2 ; Mahvi AH2, 3, 4 ; Izanloo H1 ; Ansari Tadi R5 ; Gharagazloo F6
Authors
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Authors Affiliations
  1. 1. Research Center for Environmental Pollutants, Qom University of Medical Science, Qom, Iran
  2. 2. Department of Environmental Health Engineering, School of Public Health, Tehran University of Medical Sciences, Tehran, P.O. Box: 14155-6446, Iran
  3. 3. Center for Solid Waste Research, Institute for Environmental Research, Tehran University of Medical Sciences, Tehran, Iran
  4. 4. National Institute of Health Research, Tehran University of Medical Sciences, Tehran, Iran
  5. 5. Qom Water and Wastewater Company, Qom, Iran
  6. 6. Department of Environmental Health Engineering, Kashan University of Medical Sciences, Kashan, Iran

Source: Desalination and Water Treatment Published:2016


Abstract

Traditionally, aerated lagoons are not reliable wastewater treatment systems to eliminate nutrient contents of municipal wastewater. This study aimed to enhance the aerated lagoon effluent quality by applying a simple filtration system. Removal of nitrogen and phosphorous from aerated lagoon effluent using horizontal roughing filter (HRF) was investigated. Also, the “1/3–2/3 theory” was applied to predict the TSS concentration of HRF effluent. An experimental setup of HRF was used to receive the continuous effluent from wastewater treatment plant. HRF was operated at three consecutive filtration rates, including 0.5, 1 and 1.5 m3 m−2 h−1. At the first filtration rate (0.5 m3 m−2 h−1), the removal efficiencies of total Kjeldahl nitrogen, total phosphorous, TSS, and COD were reported 50, 54, 63, and 68%, respectively. Decreasing the removal efficiency was occurred during raising the filtration rate (p < 0.05). Applying the “1/3–2/3 theory” revealed the significant correlation between predicted and measured TSS values. The capacity of HRF to retain nitrogen, phosphorous, and COD during the filtration runs was 24.3, 10.1, and 435.4 g m−3d−1, respectively. HRF can be applied as an appropriate alternative for tertiary treatment of the aerated lagoon effluent. © 2015 Balaban Desalination Publications. All rights reserved.
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