WANG Qing-liang, HU Nan, DING De-xin, ZHANG Guo-qi, HU E-ming, ZHANG Hong-can, YANG Yi-han, JIANG Xiao-hui. Removal of NO3--N From Polluted Groundwater in Decommissioned Mining Area in an In-situ Leach Uranium Mine by Denitrifying Bacteria Bioreactor[J]. Atomic Energy Science and Technology, 2013, 47(8): 1300-1306. DOI: 10.7538/yzk.2013.47.08.1300
Citation: WANG Qing-liang, HU Nan, DING De-xin, ZHANG Guo-qi, HU E-ming, ZHANG Hong-can, YANG Yi-han, JIANG Xiao-hui. Removal of NO3--N From Polluted Groundwater in Decommissioned Mining Area in an In-situ Leach Uranium Mine by Denitrifying Bacteria Bioreactor[J]. Atomic Energy Science and Technology, 2013, 47(8): 1300-1306. DOI: 10.7538/yzk.2013.47.08.1300

Removal of NO3--N From Polluted Groundwater in Decommissioned Mining Area in an In-situ Leach Uranium Mine by Denitrifying Bacteria Bioreactor

  • The pollution of groundwater by NO3- in the decommissioned mining area in an in-situ leach uranium mine is being paid more and more attention. The denitrifying bacteria by domesticating the sludge taken from the decommissioned mining area in an in-situ leach uranium mine in North West of China were obtained. An up-flow fixed-bed denitrifying bacteria bioreactor was designed. The effects of pH, the ratio of carbon to nitrogen and HRT on the removal of NO3--N from the polluted groundwater in the decommissioned mining area in the in-situ leach uranium mine by the denitrifying bacteria bioreactor were investigated. The results show that when pH, the concentration of NO3--N and HRT are set to 6.50, 1 000 mg/L and 2.3 h, respectively, the removal of the NO3--N amounts to 97%, the NO3--N degradation rate is 388 mg/(h•L) and the capacity of the bioreactor is 0.35 m3/(h•m3). When pH, the concentration of NO3--N and HRT are set to 6.50, 550 mg/L and 1.4 h, respectively, the removal of the NO3--N amounts to 96% and the capacity of the bioreactor is 0.62m3/(h•m3). The bioreactor should work on the operation conditions that pH is 5.00-8.00 and the ratio of carbon to nitrogen is 0.6-0.8.
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