Yuan Ching, Weng Chih-Huang
Department of Civil and Environmental Engineering, National University of Kaohsiung, No. 700, Kaohsiung University Road, Nan-Tzu District, Kaohsiung City 811, Taiwan, ROC.
Chemosphere. 2006 Sep;65(1):88-96. doi: 10.1016/j.chemosphere.2006.02.050. Epub 2006 Apr 27.
An enhanced electrokinetic process for removal of metals (Cr, Cu, Fe, Ni, Pb, Zn) from an industrial wastewater sludge was performed. The electrokinetic experiments were conducted under a constant potential gradient (1.25 V cm(-1)) with processing fluids of tap water (TW), sodium dodecylsulfate (SDS) and citric acid (CA) for 5 days. Results showed that metal removal efficiency of heavy metals for EK-TW, EK-SDS and EK-CA systems are 11.2-60.0%, 37.2-76.5%, and 43.4-78.0%, respectively. A highest metal removal performance was found in EK-CA system. The removal priority of investigated metals from sludge by EK process was found as: Cu > Pb > Ni > Fe > Zn > Cr. The results of sequential extraction analysis revealed that the binding forms of heavy metals with sludge after electrokinetic process were highly depend upon the processing fluid operated. It was found that the binding forms of metals with sludge were changed from the more difficult extraction type (residual and sulfate fractions) to easier extraction types (exchangeable, sorbed, and organic fraction) after treatment by electrokinetic process. Results imply that if a proper treatment technology is followed by this EK process to remove metals more effectively, this treated sludge will be more beneficial for sludge utilization afterwards. Before it was reused, the risk associated with metals of more mobile forms to the environment need to be further investigated. The cost analysis was also evaluated for the investigated electrokinetic systems.
开展了一种强化电动过程以去除工业废水污泥中金属(铬、铜、铁、镍、铅、锌)的研究。电动实验在恒定电位梯度(1.25 V cm⁻¹)下进行,处理液分别为自来水(TW)、十二烷基硫酸钠(SDS)和柠檬酸(CA),处理时间为5天。结果表明,EK - TW、EK - SDS和EK - CA体系中重金属的去除效率分别为11.2% - 60.0%、37.2% - 76.5%和43.4% - 78.0%。EK - CA体系中金属去除性能最高。通过电动过程从污泥中去除所研究金属的优先顺序为:铜>铅>镍>铁>锌>铬。连续萃取分析结果表明,电动过程后重金属与污泥的结合形态高度依赖于所使用的处理液。研究发现,电动处理后,金属与污泥的结合形态从更难萃取的类型(残渣态和硫酸盐态)转变为更易萃取的类型(可交换态、吸附态和有机态)。结果表明,如果在该电动过程之后采用适当的处理技术更有效地去除金属,那么处理后的污泥将更有利于后续的污泥利用。在污泥再利用之前,需要进一步研究更易迁移形态的金属对环境的风险。还对所研究的电动系统进行了成本分析。