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BIOLOGICAL DENITRIFICATION IN A CONTINUOUS FLOW MEMBRANE REACTOR

机译:连续流膜反应器中的生物脱氮

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Biological denitrification in a continuous flow membrane reactor has been investigated. The nitrate-laden water treated was separated from a suspended denitrifying culture by a 0.02 μm average pore diameter membrane. Equal pressure was maintained across the membrane and nitrate was removed by molecular diffusion through the membrane and into the denitrifying culture. A nitrate removal efficiency of approximately 90% or a flux of 4 g NO_3~--N/m~2/d of membrane area was achieved with an influent concentration of 20 mg/L NO_3~--N. A mathematical model was developed to approximate system performance. Predicted effluent concentrations for the experiments conducted were 5.7, 9.5, 11.7, and 17.6 mg/L NO_3~--N. The respective measured effluent concentrations were 2.3, 6.0, 9.0, and 16.0 mg/L NO_3~--N.
机译:已经研究了连续流膜反应器中的生物反硝化作用。用0.02μm平均孔径的膜将处理过的含硝酸盐的水从悬浮的反硝化培养物中分离出来。跨膜保持相等的压力,硝酸盐通过分子扩散穿过膜并进入反硝化培养物中而除去。当进水浓度为20 mg / L NO_3-N时,硝酸盐去除效率约为90%或通量为4 g NO_3-N / m〜2 / d膜面积。开发了一个数学模型来近似系统性能。所进行的实验的预计流出物浓度为5.7、9.5、11.7和17.6 mg / L NO_3-〜N。分别测得的废水浓度为2.3、6.0、9.0和16.0 mg / L NO_3-〜N。

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