4.4 Article

Electroflotation clarifier to enhance nitrogen removal in a two-stage alternating aeration bioreactor

期刊

ENVIRONMENTAL TECHNOLOGY
卷 34, 期 19, 页码 2769-2776

出版社

TAYLOR & FRANCIS LTD
DOI: 10.1080/09593330.2013.788072

关键词

wastewater treatment; alternating aeration bioreactor; electroflotation; activated sludge; nitrogen removal

资金

  1. Korea Institute of Science and Technology (KIST)
  2. Bill and Melinda Gates Foundation [OPP1037491]
  3. SNU SIR Group of the BK21 research programme
  4. Ministry of Education and Human Resources Development
  5. Bill and Melinda Gates Foundation [OPP1037491] Funding Source: Bill and Melinda Gates Foundation

向作者/读者索取更多资源

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 1.0kgm(-2). In the continuous operation of the bioreactor, the returned activated sludge concentration increased to more than 18,000mgL(-1), while the effluent suspended solids concentration was lowered below 5mgL(-1). Under influent chemical oxygen demand (COD)/total inorganic nitrogen (TIN) concentration of 300/30mgL(-1), the TIN removal efficiency was near 70% with cycle time ratios of 0.17 and 0.27. Under higher influent COD concentration of 500mgL(-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 (>6000mgL(-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 6h, even under increasing influent loadings.

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