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...

Full description

Saved in:
Bibliographic Details
Published in:Water environment research Vol. 76; no. 5; pp. 388 - 393
Main Authors: Lee, Lai Yoke, Ong, Say Leong, Ng, Wun Jern
Format: Journal Article
Language:English
Published: Alexandria, VA Water Environment Federation 01-09-2004
Blackwell Publishing Ltd
Subjects:
Online Access:Get full text
Tags: Add Tag
No Tags, Be the first to tag this record!
Description
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.
Bibliography:ObjectType-Article-1
SourceType-Scholarly Journals-1
ObjectType-Feature-2
content type line 23
ISSN:1061-4303
1554-7531
DOI:10.2175/106143004X151653