Denitrification of Nitrate Wastewater Using Packed-Bed Columns
Columnar packed-bed (PB) reactors with a specific surface area of 127${\rm m}^{2}/{\rm m}^{3}$were investigated in this study for treating nitrate wastewater. This study demonstrated that a single-stage packed bed was able to achieve total nitrogen (TN) and chemical oxygen demand (COD) removal effic...
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Published in: | Water environment research Vol. 76; no. 5; pp. 388 - 393 |
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Main Authors: | , , |
Format: | Journal Article |
Language: | English |
Published: |
Alexandria, VA
Water Environment Federation
01-09-2004
Blackwell Publishing Ltd |
Subjects: | |
Online Access: | Get full text |
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Summary: | Columnar packed-bed (PB) reactors with a specific surface area of 127${\rm m}^{2}/{\rm m}^{3}$were investigated in this study for treating nitrate wastewater. This study demonstrated that a single-stage packed bed was able to achieve total nitrogen (TN) and chemical oxygen demand (COD) removal efficiencies higher than 83 and 75%, respectively. The highest achievable TN and COD removal rates were 47.2 g${\rm N}/{\rm m}^{2}\cdot {\rm d}$and 158.0 g${\rm COD}/{\rm m}^{2}\cdot {\rm d}$, respectively. The substrate removal rate in the PB column was found to follow half-order reaction kinetics, with a reaction coefficient, k, of 53.62$({\rm mg}/{\rm L})^{1/2}/{\rm d}$. A dual-stage PB system was capable of achieving TN and COD removal efficiencies greater than 99 and 98%, respectively. Effluent TN and COD concentrations less than 6.5 mg${\rm NO}_{3}{}^{-}\text{-}{\rm N}/{\rm L}$and 50.0 mg COD/L, respectively, were obtained when the dual PB system was used. |
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Bibliography: | ObjectType-Article-1 SourceType-Scholarly Journals-1 ObjectType-Feature-2 content type line 23 |
ISSN: | 1061-4303 1554-7531 |
DOI: | 10.2175/106143004X151653 |