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受控制的序批式生物阴极反硝化用于污染地下水的生物修复。

Controlled sequential biocathodic denitrification for contaminated groundwater bioremediation.

机构信息

Department of Civil Engineering and Architecture, University of Pavia, Via Adolfo Ferrata 3, 27100 Pavia, Italy.

Department of Civil Engineering and Architecture, University of Pavia, Via Adolfo Ferrata 3, 27100 Pavia, Italy.

出版信息

Sci Total Environ. 2019 Feb 15;651(Pt 2):3107-3116. doi: 10.1016/j.scitotenv.2018.10.196. Epub 2018 Oct 15.

Abstract

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-N m d) at constant NO-N concentration (40 mgNO-N L), 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 loading rates between 66 and 200 gNO-N m d. The first stage reactor achieved lower values of effluent nitrate and nitrite than WHO guidelines for drinking water quality (<11.3 mg NO-N L, and 0.9 mgNO-N L, respectively) up to a nitrate loading rate of 167 gNO-N m d; in these conditions the second stage acted mainly as polishing step. From a loading rate of 200 gNO-N m d on, NO 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-N m 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 (SEC) and volume treated (SEC). The described combination of two bioelectrochemical systems system hence proved to be effective for groundwater denitrification.

摘要

硝酸盐地下水污染是一个全球性的问题。在本研究中,测试了一种新型的两阶段序批式生物阴极反硝化系统,以对合成地下水进行自养反硝化。该系统在不同的硝酸盐负荷率(66-301 gNO-N m d)下运行,恒NO-N浓度(40 mgNO-N L),通过在不同试验中改变水力停留时间(HRT),从大约 14 小时到 3 小时不等。当硝酸盐负荷率在 66 到 200 gNO-N m d 之间时,该系统能够实现硝酸盐(>95%)和总氮(TN)(>92%)的几乎完全去除。第一阶段反应器的出水硝酸盐和亚硝酸盐值低于世界卫生组织饮用水水质标准(<11.3 mg NO-N L,分别为 0.9 mgNO-N L),直至硝酸盐负荷率达到 167 gNO-N m d;在这些条件下,第二阶段主要作为抛光步骤。从 200 gNO-N m d 的负荷率开始,在第一阶段反应器中观察到硝酸盐积累,随后在第二阶段中成功去除。两步法的最大硝酸盐去除率为 259.83 gNO-N m,在 3.19 h 的 HRT 下。该系统的比能耗(SEC)随着 HRT 的降低而降低,无论是以去除的硝酸盐质量(SEC)还是处理的体积(SEC)计。因此,两个生物电化学系统的组合被证明对地下水脱氮有效。

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