کد مقاله | کد نشریه | سال انتشار | مقاله انگلیسی | نسخه تمام متن |
---|---|---|---|---|
681322 | 1460018 | 2012 | 11 صفحه PDF | دانلود رایگان |

In this study, a twin-chamber upflow bio-electrochemical reactor packed with palm shell granular activated carbon as biocarrier and third electrode was used for sequential nitrification and denitrification of nitrogen-rich wastewater under different operating conditions. The experiments were performed at a constant pH value for the denitrification compartment. The effect of variables, namely, electric current (I) and hydraulic retention time (HRT), on the pH was considered in the nitrification chamber. The response surface methodology was used based on three levels to develop empirical models for the study on the effects of HRT and current values as independent operating variables on NH4+–N removal. The results showed that ammonium was reduced within the function of an extensive operational range of electric intensity (20–50 mA) and HRT (6–24 h). The optimum condition for ammonium oxidation (90%) was determined with an I of 32 mA and HRT of 19.2 h.
► The sequential nitrification and denitrification accomplished in a BER.
► The GAC play key role as biocarrier and third electrode in this pattern.
► The HRT and I are important operational parameters in this system.
► The CCD and RSM declared sufficient models based on experimental results.
Journal: Bioresource Technology - Volume 125, December 2012, Pages 256–266