化学氧化耦合电动力技术修复有机污染土壤

有机污染物严重危害着我国土壤环境。探讨了电动力技术修复有机污染土壤的可行性及相关参数的变化特性,并探究了电动力修复耦合化学氧化工艺及表面活性剂辅助等多种措施对修复效果的影响。结果表明:表面活性剂辅助反应可帮助提高有机污染物溶解性与迁移性能,从而提高修复效果;采用KMn O4氧化耦合电动力工艺修复受污染高岭土时有着最佳的修复效率,污染物平均去除率可达70%。     

水中无机阳离子混凝剂的电动检测特性研究

为了在本质特征上定量说明水中无机阳离子混凝剂浓度与胶体稳定性的关系,提出了一种新的研究混凝过程胶体电荷变化的本质参数－流动电流。研究了无机阳离子混凝剂的性质和家度与电动特性参数之间的一般规律及等电点特征,考察了以ＳＣ表征混凝剂对水中胶体颗粒物作用的特性与效能,从而提出了一种研究混凝和在线监测水中胶体电荷对于混凝剂投加量变化的有效方法。     

Electrokinetic removal of chromium and copper from contaminated soils by lactic acid enhancement in the catholyte

The electrokinetic removal of chromium and copper from contaminated soils by adding lactic acid in cathode chamber as an enhancing reagent was evaluated. Two sets of duplicate experiments with chromium contaminated kaolinite and with a silty soil sampled from a supeffund site in Califomia of USA and polluted by Cr and Cu, were carried out in a constant current mode. Changes of soil water content and soil pH before and after the electrokinetic experiments, and variations of voltage drop and electroosmosis flow during the treatments were examined. The results indicated that Cr, spiked as Cr(Ⅵ) in the kaolinite, was accumulated mainly in the anode chamber, and some of Cr and metal hydroxides precipitated in the soil sections in contact with the cathode, which significantly increased electrical energy consumption. Treatment of the soil collected from the site showed accumulation of large amounts of Cr and Cu in the anode chamber while none was detected in the cathode one. The results suggested that the two metals either complexed with the injected lactic acid at the cathode or existed as negatively charged complex, and electromigrated toward the anode under a voltage gradient.     

不同的增强试剂对重金属污染场地土壤的电动修复影响

选择重金属污染场地土壤为修复对象,研究了添加络合剂EDTA?有机酸乳酸和柠檬酸以及无机酸硝酸对电动修复该污染土壤的影响.结果表明,增强试剂的加入,显著促进了铜?铅?镍和六价铬在电场中的迁移和去除,电动过程促进了土壤重金属向有效态(醋酸铵提取)转化.其中,在阴极加入乳酸并控制pH3.5的处理,土壤中铜的去除率最高,达78.7%.在阴?阳极都加入EDTA的处理中,土壤中重金属的去除率在30%左右,重金属在靠近阴极的部分发生聚集.在阴极加入柠檬酸的处理中,土壤中铜?镍和六价铬的去除率均较高,分别为68.5%?53.3%和52.9%.阴极加入硝酸控制pH3.5对土壤中六价铬的去除率最高,达93.3%.     

污染土壤电动修复增强方法研究进展

污染土壤电动修复是一项新兴绿色原位修复技术。其原理是在土壤上施加直流电场 ,利用电迁移和电渗去除污染物 ,土壤pH、Zeta电位以及土壤化学性质等因素影响电动修复效果。为了提高修复效率和扩大电动修复应用范围 ,现在已经发展了针对不同类型土壤和污染物的增强修复技术。本文归纳总结了 1995年以来土壤电动修复中常用增强处理效果的 8种方法 ,即酸碱中和法、阳离子选择膜法、电渗析法、络合剂法、表面活性剂法、氧化 还原法、EK 生物联用和LasagnaTM法 ,且对每种方法的典型实验装置、增强原理、方法特点和适用范围等进行了分析和讨论 ,为以后的实验设计提供了有益的参考     

Evaluation of Electrokinetic Remediation of Arsenic-contaminated Soils

The potential of electrokinetic (EK) remediation technology has been successfully demonstrated for the remediation of heavy metal-contaminated fine-grained soils through laboratory scale and field application studies. Arsenic contamination in soil is a serious problem affecting both site use and groundwater quality. The EK technology was evaluated for the removal of arsenic from two soil samples; a kaolinite soil artificially contaminated with arsenic and an arsenic-bearing tailing-soil taken from the Myungbong (MB) gold mine area. The effectiveness of enhancing agents was investigated using three different types of cathodic electrolytes; deionized water (DIW), potassium phosphate (KH₂PO₄) and sodium hydroxide (NaOH). The results of the experiments on the kaolinite show that the potassium phosphate was the most effective in extracting arsenic, probably due to anion exchange of arsenic species by phosphate. On the other hand, the sodium hydroxide seemed to be the most efficient in removing arsenic from the tailing-soil. This result may be explained by the fact that the sodium hydroxide increased the soil pH and accelerated ionic migration of arsenic species through the desorption of arsenic species as well as the dissolution of arsenic-bearing minerals.     

水处理氧化还原过程的电动化学特性

以流动电流为参数,研究了水处理条件下氧化还原过程的电动化学特性.考察了水中KMnO_4及其与Mn~(2+),Fe~(2+)之间氧化还原作用的流动电流(SC)规律,探讨了氧化还原的初始条件、水处理环境、原水水质、氧化剂与还原剂的投加方式等对流动电流的影响.结果表明,水中约0.5mg·l~(-1)的KMnO_4可产生SC的峰值,而且当它与Mn~(2+)和Fe~(2+)经不同条件进行氧化还原作用时,可通过SC值的变化表现出更为明显的电动化学特性.     

施加电压对铬污染土壤电动修复的影响

试验研究了不同电压条件下电动修复去除效率和单位能耗随施加电压的变化关系,探讨了电动修复经济有效的电压范围.试验选用重铬酸钾作为污染物,配制高岭土中Cr(Ⅵ)初始质量分数为100 mg/kg和500 mg/kg,含水量为50%,试验运行48 h,用乙酸控制阴极pH在4～7之间,施加一系列不同直流电压.试验结果表明,随着施加电压升高,去除效率增大,电压升高到1 V/cm时,去除效率显著升高,2种试验土壤去除效率分别为76.7%和89.8%;同时随着施加电压增加,电能消耗显著增加,与电压呈现线性递增和幂指数递增关系;综合去除效率和单位能耗2种因素,对于试验所研究的土壤,1～1.5 V/cm的电压是较为经济有效的.     

聚合铝的形态稳定性及其动电特性的研究

本文采用改进的Ａｌ－Ｆｅｒｒｏｎ快速测定法研究了混凝过程中铝盐与聚合铝水解形态的转化规律及稳定性，并对混凝反应过程中铝与聚合铝溶解－沉淀形态分布与理论溶解度进行了对比，同时采用流动电流技术直接测定了铝盐与聚合铝絮凝剂的荷电状况，最后对发生在混凝过程中铝与聚合铝最佳凝聚形态进行了讨论。     

铬-菲复合污染土壤的电动修复效果

为了解决常规电动修复方法对土壤重金属-有机物复合污染去除效率低的问题,采用向电解液中添加表面活性剂以及控制阴极电解液为酸性的电动强化修复技术,以Cr和菲为代表性污染物,研究电压和表面活性剂〔TritonX-100(曲拉通100)、SDBS(十二烷基苯磺酸钠)〕以及阴极电解液pH对修复效果的影响. 结果表明:Cr(Ⅵ)以阴离子团形式呈现向阳极迁移的趋势,菲呈现向阴极迁移的趋势;随着施加电压的升高,污染物去除率也会相应提高,当电压梯度升至1.0 V/cm时,Cr(T)、Cr(Ⅵ)、菲的去除率分别达到34.3%、76.9%、12.7%. 在电压梯度为1 V/cm的条件下,控制阴极电解液pH为4.00时,Cr(T)、Cr(Ⅵ)、菲的去除率分别升至45.1%、84.8%、23.1%;向电解液中添加表面活性剂后能提高污染物的去除率,其中,添加SDBS能够将Cr-菲复合污染土壤中Cr(T)、Cr(Ⅵ)的去除率由34.3%、76.9%升至39.9%、82.0%,添加TritonX-100能够将有机物菲的去除率由12.7%升至27.0%. 研究显示,修复处理后污染物浓度均有不同程度的降低,充分表明电动处理时提高修复电压、添加表面活性剂以及控制阴极电解液的酸碱性可以明显促进污染物在土壤中的迁移.