田家宇, 徐勇鹏, 张艳, 潘志辉, 韩正双, 李圭白. 浸没式MBR工艺应对饮用水源氨氮冲击负荷的效能[J]. 北京工业大学学报, 2012, 38(4): 636-640.
    引用本文: 田家宇, 徐勇鹏, 张艳, 潘志辉, 韩正双, 李圭白. 浸没式MBR工艺应对饮用水源氨氮冲击负荷的效能[J]. 北京工业大学学报, 2012, 38(4): 636-640.
    TIAN Jia-yu, XU Yong-peng, ZHANG Yan, PAN Zhi-hui, HAN Zheng-shuang, LI Gui-bai. Effectiveness of Submerged Membrane Bioreactor Process for Coping With Ammonium Shock Loading in Drinking Water Treatment[J]. Journal of Beijing University of Technology, 2012, 38(4): 636-640.
    Citation: TIAN Jia-yu, XU Yong-peng, ZHANG Yan, PAN Zhi-hui, HAN Zheng-shuang, LI Gui-bai. Effectiveness of Submerged Membrane Bioreactor Process for Coping With Ammonium Shock Loading in Drinking Water Treatment[J]. Journal of Beijing University of Technology, 2012, 38(4): 636-640.

    浸没式MBR工艺应对饮用水源氨氮冲击负荷的效能

    Effectiveness of Submerged Membrane Bioreactor Process for Coping With Ammonium Shock Loading in Drinking Water Treatment

    • 摘要: 在平行运行的条件下对比研究了单独的浸没式膜生物反应器(membrane bioreactor,MBR)、生物活性炭(biological activated carbon,BAC)以及BAC+MBR联用工艺应对饮用水源氨氮冲击负荷的效能.结果表明,单独的MBR具有优异的应对水源突发性氨氮污染的能力:ρ(NH3-N)在原水中为8~10 mg/L的情况下,出水中仅为(0.36±0.15)mg/L,而且出水中仅在进水ρ(NH3-N)高达9.74 mg/L时产生了短暂的NO2--N积累现象.BAC由于受到供氧能力的限制,对氨氮的去除能力有限,并且出水中始终存在NO2--N积累.而BAC+MBR联用工艺也能在氨氮冲击负荷时较好去除NH3-N,ρ(NH3-N)在原水中为8~10 mg/L时可在出水中降至(0.39±0.19)mg/L,但是出水中产生NO2--N积累的时间明显长于单独的MBR.然而,BAC+MBR联用工艺能通过两级生物屏障更好地去除水中的有机物,因此建议根据原水水质等条件选择合适的生物处理工艺.

       

      Abstract: In this investigation,the individual submerged membrane bioreactor(MBR),the biological activated carbon(BAC),and the hybrid BAC+MBR process are operated in parallel and investigated in terms of their effectiveness for coping with ammonium shock loading in drinking water sources.Experimental results show that the individual MBR exhibits excellent capacity in dealing with the sudden high-ammonium pollution,as demonstrated by the fact that even when the NH3-N concentration of 8-10 mg/L is presented in raw water,the corresponding MBR effluent concentration is only(0.36±0.15) mg/L,and the effluent NO2--N accumulation is observed only when the influent NH3-N concentration is as high as 9.74 mg/L.Due to the limited availability of dissolved oxygen in BAC,the efficiency of BAC for ammonium removal during ammonium shock loading is lower.On the other hand,excellent NH3-N removal can also be achieved using the hybrid BAC+MBR process during the sudden high-ammonium period(8-10 mg/L),with a effluent NH3-N concentration of as low as(0.39±0.19) mg/L.However,longer duration of NO2--N accumulation is detected in the hybrid BAC+MBR effluent as compared with that in individual MBR effluent.Nonetheless,the hybrid BAC+MBR process is able to remove more organic pollutants from the water through two stages of biodegradation.Thus,the suitable biological treatment process is supposed to choose according to the raw water qualities.

       

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