在大巴萨克运河(塞尔维亚)沉积物的电动修复过程中锌、镍、铜和镉的行为。
Behavior of zinc, nickel, copper and cadmium during the electrokinetic remediation of sediment from the Great Backa Canal (Serbia).
机构信息
Department for Chemistry, Biochemistry and Environmental Protection, Faculty of Sciences, Novi Sad, Republic of Serbia.
出版信息
J Environ Sci Health A Tox Hazard Subst Environ Eng. 2010 Jan;45(9):1134-43. doi: 10.1080/10934529.2010.486347.
This paper describes a bench-scale study dealing with the removal of heavy metals by electrokinetic (EK) remediation from sediment of the Great Backa Canal (Vojvodina, Republic of Serbia), with an emphasis on the dependence of removal efficacies on the physicochemical states of the heavy metals and sediment chemistry. Sediment samples were spiked with the following heavy metals (mg kg(-1)): Zn 4400, Ni 900, Cu 1140 and Cd 57. In addition to determining the pseudo-total metal content in the contaminated sediment before and after EK treatment, BCR sequential extraction was also performed to examine the distribution of the contaminants in the sediment. Conventional EK remediation (EXP I) was ineffective in removing the heavy metals investigated, so two enhanced processes were developed. In both these processes, the mass of treated sediment was reduced to avoid the presence of inactive electric field areas in the sediment and increase current density. The first enhanced experiment (EXP II) used acetic acid (HAc) solution (pH 2.9) as an anolyte. Combined with the smaller sediment mass, this resulted in an increase in overall removal efficacies (9% for Zn, 15% for Ni, 10% for Cu and 15% for Cd). The second enhanced experiment (EXP III), as well as using HAc solution as an anolyte, made use of a cation exchange membrane in the cathodic chamber to minimize pH changes in the region adjacent to the cathode, which negatively influenced the removal of some heavy metals. However, no improvement in removal efficacy was achieved in EXP III. Since the redox potential of the sediment drops during the EK process, metals removal is limited by the formation of their sulfides. In conclusion, the removal of heavy metals by EK remediation is governed by a complex interplay of the complexation, precipitation and reduction processes, and the difficulties encountered in their optimization can explain the unsatisfactory effectiveness achieved by the described remediation procedure. Improved understanding of the behavior of metal ions during EK treatment can be useful in predicting and enhancing the efficacy of the process.
本文描述了一项针对大巴萨运河(塞尔维亚伏伊伏丁那自治省)底泥中重金属的电动力学(EK)修复去除的中试研究,重点关注重金属和底泥化学的物理化学状态对去除效率的依赖性。底泥样品中添加了以下重金属(mg kg(-1)):Zn 4400、Ni 900、Cu 1140 和 Cd 57。除了在 EK 处理前后测定受污染底泥中重金属的总量外,还进行了 BCR 顺序提取,以研究污染物在底泥中的分布。常规 EK 修复(EXP I)对所研究重金属的去除无效,因此开发了两种增强工艺。在这两种工艺中,处理底泥的质量都减少了,以避免底泥中存在无效电场区域,并提高电流密度。第一个增强实验(EXP II)使用乙酸(HAc)溶液(pH 2.9)作为阳极电解液。与较小的底泥质量相结合,这导致整体去除效率提高(Zn 提高 9%、Ni 提高 15%、Cu 提高 10%、Cd 提高 15%)。第二个增强实验(EXP III)除了使用 HAc 溶液作为阳极电解液外,还在阴极室中使用阳离子交换膜,以最大限度地减少阴极附近区域的 pH 变化,这对某些重金属的去除产生负面影响。然而,在 EXP III 中没有提高去除效率。由于 EK 过程中底泥的氧化还原电位下降,金属的去除受到其硫化物形成的限制。总之,EK 修复中重金属的去除受到络合、沉淀和还原过程的复杂相互作用的控制,在优化过程中遇到的困难可以解释所描述的修复程序的效果不佳。更好地了解金属离子在 EK 处理过程中的行为有助于预测和提高该过程的效率。