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Simultaneous Removal of Pb, Cd, and Zn from Heavily Contaminated Mine Tailing Soil Using Enhanced Electrochemical Process

机译:使用增强的电化学工艺同时除去Pb,Cd和Zn的污染矿井尾矿土壤

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This study examined the efficacy of electrokinetic remediation of chelated mine tailing soils with mixed heavy metals. Electrokinetic experiments were conducted in a nontraditional bench-reactor that contained intermediate liquid collection interfaces within treatment zones between the electrodes. Tests were conducted using 0.05 M Na(2)EDTA as the chelating permeant. Tap water was used in control experiments. A constant direct current voltage of 20 V (electric field approximate to 0.625 V/cm) was applied across working electrodes for 48 h. Transient and spatial distribution of pH, conductivity, oxidation-reduction potential (E-h), and cumulative mass of the metal species in solution were measured. In all experiments, including controls, a larger portion of soluble metals were found in the anode reservoir, indicating transformation of the metals into complex species of negative charge, reverse electroosmotic advection toward anode, and/or colloidally assisted transport. Na(2)EDTA was expected to increase the metal extraction into the analyte as it produced negatively charged complexes with the metals. Soluble mass of the metals was markedly low in the catholyte, with heavy precipitation of metal hydroxide salts in the ensuing high pH, low E-h environment. Total removals of all three metals were either unchanged or lower, for the same duration of treatment with 0.05 M Na(2)EDTA than with tap water. Results showed that chelating agents, as was exemplified with a commonly used ligand in here, may not be advantageous in enhancing electrokinetic remediation of heavily contaminated mine tailings. In such substrates, metals' transport and removal regime (i.e., rate, sequence and preference of extraction) appeared to be influenced more so by the type of metal and transient distribution of the pH-E-h under the electric field than the solubilizing effect of a ligand within the treatment zone.
机译:本研究检测了螯合矿尾土壤与混合重金属螯合矿尾土的疗效。电动实验在非传统的支撑反应器中进行,该反应器包含在电极之间的治疗区内的中间液体收集界面。使用0.05M Na(2)EDTA作为螯合渗透进行测试。自来水用于对照实验。在工作电极上施加48小时的工作电极施加20V的恒定直流电压(电场近似为0.625 V / cm)。测定pH,电导率,氧化还原电位(E-H)和溶液中金属物种的累积质量的瞬态和空间分布。在所有实验中,包括对照,在阳极储存器中发现较大部分的可溶性金属,将金属的转化成复杂的负电荷物种,对阳极的反向电渗透压平流和/或胶体辅助运输。预期Na(2)EDTA预计将金属萃取增加到分析物中,因为它产生带负电荷的配合物与金属产生带负电的配合物。在阴极电解液中,金属的可溶物质量显着低,在随后的高pH值低,E-H环境中具有重度氢氧化物盐的沉淀。对于所有三种金属的总去除去,或更低,对于含有0.05M Na(2)EDTA的持续时间,而不是自来水。结果表明,与此处的常用配体举例说明的螯合剂可能在增强重污染的矿井尾矿的电动修复方面是有利的。在这种基板中,金属的运输和去除制度(即,萃取的速率,序列和偏好)似乎通过电场下的金属类型和PH-EH的瞬态分布而受到比A的溶解作用的影响更多治疗区内的配体。

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