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Nitrate removal from drinking water using a membrane-fixed biofilm reactor

机译:使用膜固定式生物膜反应器从饮用水中去除硝酸盐

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摘要

Biological treatment of drinking water is a cost-effective alternative to conventional physico/chemical processes. A new concept was tested to overcome the main disadvantage of biological denitrification, the intensive post-treatment process to remove microorganisms and remnant carbon source. The biological reaction zone and carbon supply were separated from the raw water stream by a nitrate-permeable membrane. Denitrification takes place in a biofilm, which is immobilized at the membrane. In a series of bench-scale runs, different types of membranes and reactor configurations were investigated. The best denitrification rates achieved were 1230 mg NO3(-)-N m-2 day-1. In one run, raw water containing 100 mg NO3- 1-1 was completely freed from nitrate. The membrane and the attached biofilm also represent a barrier against the passage of the C source and nutrients into the raw water. At concentrations of 20 mg 1-1 ethanol and 15 mg 1-1 phosphate in the bioreactor no diffusion through the membrane into the treated water was observed. Without any post-treatment, the effluent met nearly all the relevant criteria for drinking water; only the colony count was slightly increased.
机译:饮用水的生物处理是传统物理/化学过程的一种经济有效的替代方法。测试了一个新概念,以克服生物反硝化的主要缺点,这是去除微生物和残余碳源的密集后处理过程。通过硝酸盐可渗透膜将生物反应区和碳供应与原水分离。反硝化作用发生在固定在膜上的生物膜中。在一系列实验规模的运行中,研究了不同类型的膜和反应器配置。达到的最佳反硝化速率为1230 mg NO3(-)-N m-2 day-1。在一次运行中,完全清除了包含100 mg NO3-1-1的原水。膜和附着的生物膜也代表了阻止碳源和养分进入原水中的屏障。在生物反应器中浓度为20 mg 1-1乙醇和15 mg 1-1磷酸盐时,未观察到通过膜扩散到处理过的水中。未经任何后处理,废水几乎满足所有相关的饮用水标准;只有菌落数略有增加。

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