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利用硝酸盐作为电子受体进行自养反硝化去除工业废水中的硫化物。

Sulfide removal from industrial wastewaters by lithotrophic denitrification using nitrate as an electron acceptor.

机构信息

Department of Environmental Engineering, Kocaeli University, 41380 Kocaeli, Turkey.

出版信息

Water Sci Technol. 2010;62(10):2286-93. doi: 10.2166/wst.2010.545.

DOI:10.2166/wst.2010.545
PMID:21076214
Abstract

Sulfide is present in wastewaters as well as in biogas and can be removed by several physicochemical and biotechnological processes. Nitrate is a potential electron acceptor, readily available in most wastewater treatment plants and it can replace oxygen under anoxic conditions. A lab-scale reactor was operated for treatment of sulfide containing wastewater with nitrate as an electron acceptor and is used to evaluate the effects of volumetric loading rates, hydraulic retention time (HRT) and substrate concentrations on the performance of the lithotrophic denitrification process for treating industrial fermentation wastewaters. Sulfide is removed more than 90% at the loading rates between 0.055 and 2.004 kg S(-2)/m(3) d, when the influent sulfide concentration is kept around 0.163 kg/m(3) and the HRT decreased from 86.4 to 2 h. Nitrogen removal differed between 23 and 99% with different influent NO(3)(-)-N concentration and loading rates of NO(3)(-)/S(-2) ratio. The stoichiometry of sulfide oxidation with nitrate is calculated assuming different end-products based on thermodynamic approach and compared with experimental yield values. The calculated maximum volumetric and specific sulfide oxidation rates reached 0.076 kg S(-2)/m(3) h and 0.11 kg S(-2)/kg VSS h, respectively. The results are obtained at industrially relevant conditions and can be easily adapted to either biogas cleaning process or to sulfide containing effluent streams.

摘要

硫化物存在于废水中以及沼气中,可以通过几种物理化学和生物技术过程去除。硝酸盐是一种潜在的电子受体,在大多数污水处理厂中都很容易获得,并且在缺氧条件下可以替代氧气。一个实验室规模的反应器用于处理含有硝酸盐作为电子受体的含硫废水,用于评估容积负荷率、水力停留时间 (HRT) 和基质浓度对用于处理工业发酵废水的自养反硝化过程性能的影响。当进水硫化物浓度保持在 0.163kg/m³左右,HRT 从 86.4 小时降低到 2 小时时,在 0.055 至 2.004kg S(-2)/m³·d 的负荷率下,硫化物去除率超过 90%。不同的进水 NO(3)(-)-N 浓度和 NO(3)(-)/S(-2) 比的负荷率下,氮去除率在 23%至 99%之间有所不同。基于热力学方法假设不同的最终产物,计算了硝酸盐氧化硫化物的化学计量比,并与实验产率值进行了比较。计算出的最大体积和特定硫化物氧化速率分别达到 0.076kg S(-2)/m³·h 和 0.11kg S(-2)/kg VSS·h。这些结果是在工业相关条件下获得的,可以很容易地适应沼气净化过程或含有硫化物的废水排放。

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