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在填充有铁涂覆砂和锰涂覆砂的柱式反应器中去除三价砷。

Removal of As(III) in a column reactor packed with iron-coated sand and manganese-coated sand.

作者信息

Chang Yoon-Young, Song Ki-Hoon, Yang Jae-Kyu

机构信息

Department of Environmental Engineering, Kwangwoon University, Seoul 139-701, Republic of Korea.

出版信息

J Hazard Mater. 2008 Feb 11;150(3):565-72. doi: 10.1016/j.jhazmat.2007.05.005. Epub 2007 May 10.

Abstract

The applicability of manganese-coated sand (MCS) and iron-coated sand (ICS) for the treatment of As(III) via oxidation and adsorption processes was investigated. Scanning electron microscopy (SEM) and X-ray diffraction spectroscopy (XRD) were used to observe the surface properties of the coated layer. In the batch adsorption, the adsorption rate of As(V) onto ICS was greater than that of As(III), and ICS showed a greater adsorption capacity for the removal of As(V) than As(III). From a bench-scale column test, a column reactor packed with both MCS and ICS was found to be the best system for the treatment of As(III) due to the promising oxidation efficiency of As(III) to As(V) by MCS and adsorption of As(V) by both MCS and ICS. From these bench-scale results, the treatment of synthetic wastewater contaminated with As(III) was investigated using a pilot-scale filtration system packed with equal amounts (each 21.5 kg) of MCS at the bottom and ICS on the top. The height and diameter of the column were 200 and 15 cm, respectively. As(III) solution was introduced into the bottom of the filtration system, at a speed of 5 x 10(-3)cms(-1), over 148 days. The breakthrough of total arsenic in the mid-sampling (end of the MCS bed) and final-sampling (end of the ICS bed) positions began after 18 and 44 days, respectively, and showed complete breakthrough after 148 days. Although the breakthrough of total arsenic in the mid-sampling position began after 18 days, the concentration of As(III) in the effluent was below 50 microg L(-1) for up to 61 days. This result indicates that MCS has sufficient oxidizing capacity for As(III), and 1 kg of MCS can oxidize 93 mg of As(III) for up to 61 days. When the complete breakthrough of total arsenic occurred, the total arsenic removed by 1 kg of MCS was 79.0 mg, suggesting MCS acts as an adsorbent for As(V), as well as an oxidant for As(III). From this work, a filtration system consisting of both MCS and ICS can potentially be used a new treatment system to simultaneously treat As(III) and As(V).

摘要

研究了锰涂层砂(MCS)和铁涂层砂(ICS)通过氧化和吸附过程处理As(III)的适用性。采用扫描电子显微镜(SEM)和X射线衍射光谱(XRD)观察涂层的表面性质。在间歇吸附中,As(V)在ICS上的吸附速率大于As(III),并且ICS对去除As(V)的吸附容量大于As(III)。通过小型柱试验发现,填充MCS和ICS的柱式反应器是处理As(III)的最佳系统,因为MCS对As(III)氧化为As(V)具有良好的氧化效率,且MCS和ICS都能吸附As(V)。基于这些小型试验结果,使用底部填充等量(各21.5 kg)MCS且顶部填充ICS的中试规模过滤系统,对受As(III)污染的合成废水进行处理研究。柱的高度和直径分别为200 cm和15 cm。在148天内,以5×10⁻³ cm s⁻¹的速度将As(III)溶液引入过滤系统底部。总砷在中间采样(MCS床层末端)和最终采样(ICS床层末端)位置的穿透分别在18天和44天后开始,并在148天后出现完全穿透。尽管中间采样位置的总砷在18天后开始穿透,但流出物中As(III)的浓度在长达61天的时间内低于50 μg L⁻¹。该结果表明MCS对As(III)具有足够的氧化能力,1 kg MCS在长达61天的时间内可氧化93 mg As(III)。当总砷完全穿透时,1 kg MCS去除的总砷为79.0 mg,这表明MCS不仅是As(III)的氧化剂,也是As(V)的吸附剂。基于这项研究,由MCS和ICS组成的过滤系统有可能作为一种新的处理系统,同时处理As(III)和As(V)。

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