| Article ID | Journal | Published Year | Pages | File Type |
|---|---|---|---|---|
| 4409673 | Chemosphere | 2013 | 8 Pages |
Anaerobic sludge digester supernatant characterized by 569 mg TKN L−1, high color and a COD/N ratio of 1.4 was treated in granular sequencing batch reactors (GSBRs) followed by post-denitrification (P-D) and ultrafiltration (UF) steps. The use of granular sludge allowed for the oxidation of ammonium in anaerobic digester supernatant at all investigated GSBR cycle lengths of 6, 8 and 12 h. The highest ammonium removal rate (15 mg N g−1 VSS h−1) with removal efficiency of 99% was noted at 8 h.Since the GSBR effluent was characterized by a high concentration of nitrites, slowly-degradable substances and biomass, additional purification steps were applied. In P-D stage, the microbial activity of granular biomass in the GSBR effluent was implemented. The P-D was supported by external carbon source addition and the most advantageous variant comprised dosing of half of the theoretical acetate dose for nitrite reduction in the 3-h intervals. The use of the system consisting of the GSBR with 8 h, an optimal P-D variant and a UF for the treatment of anaerobic digester supernatant allowed for the 99%, 71% and 97% reductions of TKN, COD and color, respectively.
► In granular sludge batch reactor (GSBR) full nitritation in anaerobic digester supernanat (570 mg TKN L−1) was obtained. ► Structure of obtained granules ensured 20% denitrification in GSBR despite constant aeration. ► Biomass from GSBR effluent was successfully implemented in post-denitrification (P-D) stage. ► GSBR, P-D and ultrafiltration ensured 99%, 71% and 97% of TKN, COD and color removal in anaerobic digester supernanat.
