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首页> 外文期刊>The Science of the Total Environment >Controlled sequential biocathodic denitrification for contaminated groundwater bioremediation
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Controlled sequential biocathodic denitrification for contaminated groundwater bioremediation

机译:受到污染的地下水生物修复的顺序生物疗法反硝化

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Nitrate groundwater contamination is a worldwide concern. In this study, a novel 2-stage, sequential biocathodic denitrification system was tested to perform autotrophic denitrification of synthetic groundwater. The system was operated at different nitrate loading rates (66-301 gNO(3)(-)-N m(NCC)(-3) d(-)(1)) at constant NO3- -N concentration (40 mgNO(3)(-)-N L-1), by varying hydraulic retention time (HRT) during different trials from about 14 to 3 h. The system was able to achieve almost complete removal of nitrate (95%) and Total Nitrogen (TN) (92%) at NO(3)(- )loading rates between 66 and 200 gNO(3)(-)-Nm(NCC)(-3) d(-1). The first stage reactor achieved lower values of effluent nitrate and nitrite than WHO guidelines for drinking water quality (11.3 mg NO3--N L-1, and 0.9 mgNO(2)(-)-N L-1, respectively) up to a nitrate loading rate of 167 gNO(3)(-)-Nm(NCC)(-3)d(-1); in these conditions the second stage acted mainly as polishing step. From a loading rate of 200 gNO(3)(-)-Nm( Ncc)(-3)d(-1) on, N2O accumulation was observed in the first stage reactor, afterwards successfully removed in the second stage. Maximum nitrate removal rate of the 2-step process was 259.83 gNO(3)(-)-Nm(NCC)( )(-3)at HRT of 3.19 h. The specific energy consumption of the system (SEC) decreased with decreasing HRT, both in terms of mass of nitrate removed (SECN) and volume treated (SECv). The described combination of two bioelectrochemical systems system hence proved to be effective for groundwater denitrification. (C) 2018 Elsevier B.V. All rights reserved.
机译:硝酸盐地下水污染是一个全世界的关注点。在该研究中,测试了一种新的2阶段顺序生物疗法脱氮系统,以进行合成地下水的自养反脱氮。该系统以不同的硝酸盐加载速率(66-301gNO(3)( - ) - N m(NCC)( - 3)D(1))以恒定的NO 3 -N浓度(40 mgNO(3 )( - ) - n L-1),通过在不同试验期间改变液压保留时间(HRT),约14至3小时。该系统能够在NO(3)( - )加载速率下几乎完全除去硝酸盐(> 95%)和总氮(TN)(> 92%)在66和200gno(3)( - ) - nm之间的加载速率(NCC)( - 3)D(-1)。第一阶段反应器达到硝酸盐和亚硝酸盐的较低值,而不是饮用水质指令(分别为0.9 mgNO( - ) - n L-1),达到饮用水质量(<11.3毫克NO3-n L-1,分别)硝酸盐加载速率为167GNO(3)( - ) - NM(NCC)( - 3)D(-1);在这些条件下,第二阶段主要作为抛光步骤作用。从200GNO(3)( - ) - NM(NCC)( - 3)D(-1)的加载速率ON,在第一阶段反应器中观察到N2O积聚,然后在第二阶段成功除去。 2步工艺的最大硝酸盐去除率为259.83GNO(3)( - ) - NM(NCC)()( - 3),HRT为3.19小时。系统(SEC)的特定能量消耗随着HRT的降低而降低,两者在除去硝酸盐(SECN)和体积处理(SECV)方面。所描述的两个生物电化学系统系统的组合因此证明是对地下水反硝化有效的。 (c)2018年elestvier b.v.保留所有权利。

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