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在全面曝气和快速过滤过程中低浓度砷的命运。

Fate of low arsenic concentrations during full-scale aeration and rapid filtration.

机构信息

Delft University of Technology, Faculty of Civil Engineering and Geosciences, Stevinweg 1, 2628 CN Delft, The Netherlands.

Delft University of Technology, Faculty of Civil Engineering and Geosciences, Stevinweg 1, 2628 CN Delft, The Netherlands.

出版信息

Water Res. 2016 Jan 1;88:566-574. doi: 10.1016/j.watres.2015.10.034. Epub 2015 Oct 21.

Abstract

In the Netherlands, groundwater treatment commonly consists of aeration, with subsequent sand filtration without using chemical oxidants like chlorine. With arsenic (As) concentrations well below the actual guidelines of 10 μg As/L, groundwater treatment plants have been exclusively designed for the removal of iron (Fe), manganese and ammonium. The aim of this study was to investigate the As removal capacity at three of these groundwater treatment plants (10-26 μg As/L) in order to identify operational parameters that can contribute to lowering the filtrate As concentration to <1 μg/L. For this purpose a sampling campaign and experiments with supernatant water and hydrous ferric oxide (HFO) flocs were executed to identify the key mechanisms controlling As removal. Results showed that after aeration, As largely remained mobile in the supernatant water; even during extended residence times only 20-48% removal was achieved (with 1.4-4.2 mg/L precipitated Fe(II)). Speciation showed that the mobile As was in the reduced As(III) form, whereas, As(V) was readily adsorbed to the formed HFO flocs. In the filter bed, the remaining As(III) completely oxidized within 2 min of residence time and As removal efficiencies increased to 48-90%. Filter grain coating analysis showed the presence of manganese at all three treatment plants. It is hypothesized that these manganese oxides are responsible for the accelerated As(III) oxidation in the filter bed, leading to an increased removal capacity. In addition, pH adjustment from 7.8 to 7.0 has been found to improve the capacity for As(V) uptake by the HFO flocs in the filter bed. The overall conclusion is, that during groundwater treatment, the filter bed is crucial for rapid As(III) removal, indicating the importance to control the oxidation sequence of Fe and As for improved As removal efficiencies.

摘要

在荷兰,地下水处理通常包括曝气,随后进行砂滤,而不使用氯气等化学氧化剂。由于砷(As)浓度远低于实际的 10μg/L 指导值,地下水处理厂专门设计用于去除铁(Fe)、锰和铵。本研究的目的是在三个这样的地下水处理厂(10-26μg/L)中研究 As 的去除能力,以确定有助于将滤出液 As 浓度降低到 <1μg/L 的操作参数。为此,进行了采样活动,并对上清液和水合氧化铁(HFO)絮体进行了实验,以确定控制 As 去除的关键机制。结果表明,曝气后,As 主要仍在上清液中保持迁移性;即使延长停留时间,也只能实现 20-48%的去除率(沉淀 Fe(II) 为 1.4-4.2mg/L)。形态分析表明,可迁移的 As 呈还原态 As(III),而 As(V)则很容易被形成的 HFO 絮体吸附。在滤床中,剩余的 As(III)在 2 分钟的停留时间内完全氧化,As 的去除效率提高到 48-90%。滤床颗粒涂层分析表明,所有三个处理厂都存在锰。据推测,这些锰氧化物是导致滤床中 As(III)快速氧化的原因,从而提高了去除能力。此外,发现将 pH 值从 7.8 调整到 7.0 可提高 HFO 絮体在滤床中对 As(V)的吸收能力。总的结论是,在地下水处理过程中,滤床对于快速去除 As(III)至关重要,这表明控制 Fe 和 As 的氧化顺序对于提高 As 去除效率非常重要。

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