Electroflotation clarifier to enhance nitrogen removal in a two-stage alternating aeration bioreactor
Stringent water treatment criteria and rapidly growing pollutant loads provoke the demand for retrofitting wastewater treatment plants towards a higher capacity. In this study, we assess a two stage alternating aeration (AA) bioreactor equipped with electroflotation (EF) clarifier, for nitrogen remo...
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Published in: | Environmental technology Vol. 34; no. 19; pp. 2765 - 2772 |
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Main Authors: | , , , , |
Format: | Journal Article |
Language: | English |
Published: |
Abingdon
Taylor & Francis
01-10-2013
Taylor & Francis Ltd |
Subjects: | |
Online Access: | Get full text |
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Summary: | Stringent water treatment criteria and rapidly growing pollutant loads provoke the demand for retrofitting wastewater treatment plants towards a higher capacity. In this study, we assess a two stage alternating aeration (AA) bioreactor equipped with electroflotation (EF) clarifier, for nitrogen removal within a short hydraulic reTENTion time (HRT). The EF under steady solids loading required a minimum unit height and gas:solids ratio of 0.006 for efficient clarification. The separated sludge blanket was further thickened with retaining stability when the cyclic solids loading was smaller than 1.0 kg m ⁻². In the continuous operation of the bioreactor, the returned activated sludge concentration increased to more than 18,000 mg L ⁻¹, while the effluent suspended solids concentration was lowered below 5 mg L ⁻¹. Under influent chemical oxygen demand (COD)/total inorganic nitrogen (TIN) concentration of 300/30 mg L ⁻¹, the TIN removal efficiency was near 70% with cycle time ratios of 0.17 and 0.27. Under higher influent COD concentration of 500 mg L ⁻¹, TIN removal efficiency was found to be 73.4% at a carbon:nitrogen (C:N) ratio of 10 and even higher (80.4%) at a C:N ratio of 16.6. The increased mixed liquor suspended solids concentrations (>6000 mg L ⁻¹) under the high COD loading were efficiently maintained by using the EF clarifier. The results of this study demonstrate that an EF clarifier with a HRT of less than 1 h can support reliable nitrogen removal in the AA process that has a HRT of 6 h, even under increasing influent loadings. |
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Bibliography: | http://dx.doi.org/10.1080/09593330.2013.788072 ObjectType-Article-1 SourceType-Scholarly Journals-1 ObjectType-Feature-2 content type line 23 |
ISSN: | 1479-487X 0959-3330 1479-487X |
DOI: | 10.1080/09593330.2013.788072 |