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Biological denitrification of brines from membrane treatment processes using an upflow sludge blanket (USB) reactor

机译:使用上流污泥层(USB)反应器对膜处理工艺中的盐水进行生物脱氮

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This paper investigates denitrification of brines originating from membrane treatment of groundwater in an upflow sludge blanket (USB) reactor, a biofilm reactor without carrier. A simulated brine wastewater was prepared from tap water and contained a nitrate concentration of 125 mg/l as N and a total salt concentration of about 1%. in order to select for a suitable energy source for denitrification, two electron donors were compared: one promoting precipitation of calcium compounds (ethanol), while the other (acetic acid), no precipitation was expected. After extended operation to reach steady state, the sludge from the two reactors showed very different mineral contents. The VSS/TSS ratio in the ethanol fed reactor was 0.2, i.e., 80% mineral content, while the VSS/TSS ratio in the acetic acid fed reactor was 0.9, i.e., 10% mineral content. in spite of the low mineral content, the sludge from the acetic acid fed reactor showed remarkably excellent granulation and settling characteristics. Although the denitrification performance of the acetic acid fed reactor was similar to that of the ethanol fed reactor, there was a huge difference in the sludge production due to mineral precipitation, with the corresponding negative aspects including increased costs of sludge treatment and disposal and moreover, instability and difficulties in reactor operation (channeling). These arguments make acetic acid a much more suitable candidate for brine denitrification, despite previous findings observed in groundwater dentrification regarding the essential role of a relatively high sludge mineral fraction for stable and effective USB reactor operation. Based on a comparison between two denitrification reactors with and without salt addition and using acetic acid as the electron donor, it was concluded that the reason for the excellent sludge settling characteristics found in the acetic acid fed reactor is the positive effects of higher salinity on granular sludge formation.
机译:本文研究了上流污泥床(USB)反应器(一种没有载体的生物膜反应器)中对地下水进行膜处理产生的盐水的反硝化作用。用自来水制备了模拟的盐水废水,其硝酸盐浓度为N浓度为125 mg / l,总盐浓度约为1%。为了选择合适的反硝化能源,比较了两个电子给体:一个电子给体促进钙化合物(乙醇)的沉淀,而另一个电子给体(乙酸)促进沉淀,预计没有沉淀。延长运行达到稳态后,两个反应器的污泥显示出非常不同的矿物质含量。乙醇进料反应器中的VSS / TSS比为0.2,即80%的矿物质含量,而乙酸进料反应器中的VSS / TSS比为0.9,即10%的矿物质含量。尽管矿物质含量低,但乙酸进料反应器中产生的污泥仍具有出色的造粒和沉降特性。尽管乙酸进料反应器的反硝化性能与乙醇进料反应器的反硝化性能相似,但是由于矿物沉淀,污泥产量存在巨大差异,相应的负面影响包括污泥处理和处置成本的增加,此外,反应堆运行(通道)的不稳定和困难。这些观点使乙酸成为盐水反硝化的一种更合适的候选方法,尽管先前在地下水的硝化过程中观察到了相对较高的污泥矿物组分对于稳定和有效的USB反应器运行所起的重要作用。根据两个加盐和不加盐的反硝化反应器之间的比较,并使用乙酸作为电子给体,可以得出结论,在乙酸进料反应器中发现出色的污泥沉降特性的原因是较高盐度对颗粒的积极影响。污泥形成。

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