Prediction and minimization of vertical migration of DNAPLS using surfactant enhanced aquifer remediation at neutral buoyancy

Surfactant enhanced aquifer remediation (SEAR) had previously been thought to require a capillary barrier below the contaminated zone to prevent the vertical migration of a microemulsion containing solubilized DNAPL. This paper shows the vertical migration of the dense microemulsion is described and predicted by the value of three dimensionless scaling groups. Embedded within these scaling groups are four design parameters. The value of these parameters can be manipulated in order to reduce the amount of vertical migration anticipated for a given remediation design. Plots have been constructed that illustrate the relationship between vertical migration and the value of the scaling groups; such plots can be used to predict vertical migration and to determine appropriate screen intervals of extraction wells to ensure full capture of the contaminants. This predictive capability has been verified in laboratory experiments. Predicted migration of the microemulsion agreed within about 2% of that observed. Development of the scaling groups is presented, remediation design implications are discussed, and laboratory verification is shown. Additional discussion of the laboratory work is given in a companion paper [Kostarelos, K., Pope, G.A., Rouse, B.A., Shook, G.M., 1998. A new concept: the use of neutrally-buoyant microemulsions for DNAPL remediation, J. Contam. Hydro., this edition].     

电极尺寸对介质阻挡放电冷等离子体去除NO的影响

设计了一套高压电源装置以及相应的同轴圆柱 筒介质阻挡放电管 ,研究了放电管中心电极直径以及介质层管内径变化对放电冷等离子体去除NO的影响。实验结果表明 ,这 2种电极尺寸的变化对NO去除率有显著的影响。中心电极直径的增加 ,有助于增强放电 ,但同时减小了反应空间 ;介质层管内径增加 ,延长停留时间的同时放电的强度却相应减弱了。所以中心电极的直径或介质层的内径均应有一最佳值 ,使得其他条件不变的情况下NO的去除效果最佳。     

三维三相流化床电极处理苯胺实验研究

使用了一种新型的电化学反应器———三维三相流化床电极用于处理苯胺的实验研究。得到了气量大小、外加电压、电介质浓度、pH值、原水浓度、反应时间等因素对苯胺溶液COD去除率的影响规律 ,并对之进行了合理的解释和分析。结果表明 ,用三维三相流化床电极 ,在一定条件下 ,苯胺可基本被全部氧化。初步论证了苯胺电解过程中有中间产物的生成。     

微库仑法和离子色谱法测定土壤中可吸附有机卤素

采用振荡吸附处理土壤样品,用微库仑法和离子色谱法分别测定土壤中的可吸附有机卤素(AOX)。通过优化样品前处理条件以提高AOX的提取效率,上述两种方法检出限分别为15.3 mg/kg和16.3 mg/kg, 4-氯苯酚作为标准物质的加标回收率分别为92.2%～95.0%和77.7%～80.2%。两种方法测定实际土壤样品中AOX,6次测定结果的RSD为5.4%～19.2%。GSS系列标准土壤试验结果表明,振荡吸附处理样品,用微库仑法和离子色谱法在测定样品中AOX时测定结果区别不大,土壤中AOX含量与卤素含量无直接关系。     

MnOX/ACF低温选择性催化还原烟气中的NO

进行了MnOX/ACF(活性炭纤维)对低温选择性催化还原(SCR)NO的影响研究.实验表明,ACF先经浓酸预氧化,然后再负载MnOX催化剂,对NO脱除率的提高较明显,并且以20%(质量分数)HNO3预氧化处理的效果最佳.比较了相同制备条件和相同负载量下的MnOX/ACF和V2O5/ACF的催化效果,认为在同等条件下MnOX的活性高于V2O5.考察了不同负载量的MnOX对NO脱除率的影响,较理想的MnOX负载量为12%(质量分数).在此基础上就不同的催化剂质量和烟气流速比(W/F)对NO脱除率的影响进行了研究,结果表明,在低温、W/F为2～3 mg/(mL·min-1)时NO的去除率较高.     

三维电极-Fenton试剂耦合法去除废水COD实验研究

以对苯二酚模拟废水为处理对象,研究了三维电极-Fenton试剂耦合法,并对三维电极法、Fenton法及三维电极-Fenton试剂耦合法去除废水COD的效率进行了对比,结果表明,三维电极-Fenton试剂耦合法处理效率明显高于普通Fenton法和三维电极法.且最佳工艺条件下,三维电极-Fenton试剂耦合法对模拟对苯二酚废水COD去除率可达92.03%.     

PbO2电极的改性及其在难降解有机废水电化学处理中的应用

电化学方法处理难降解有机废水是一种很有前途的技术,其应用的关键是开发出高效、稳定、低成本的电极材料.PbO2电极在工业领域具有广泛的应用基础,具有较高的析氧电势和电催化活性,被认为在电化学处理难降解有机废水方面有重要的应用前景.本文对PbO2电极制备方法与改性以及在难降解有机废水电化学处理中应用的研究成果和最新进展进行了综述,并对该研究领域今后的发展趋势进行了分析.     

钛基Sn或Pb 氧化物涂层电极的制备与表征

采用热分解和电沉积方法分别制备了Ti/SnO2-Sb2O3,Ti/PbO2 和Ti/SnO2-Sb2O3/PbO2 三种电极.电镜照片表明,与热分解制备的Ti/SnO2-Sb2O3 电极表面呈"泥裂状"不同,电沉积Ti/PbO2 电极表面呈典型金刚石型结构;Ti/SnO2-Sb2O3/PbO2 电极的氧化物中间层使PbO2 结晶显著减小,而且增加了镀层PbO2 与钛基的结合力,在连续使用较长时间后电极表面出现"蜂窝状"腐蚀坑.EDAX和XRD 分析表明,虽然电极用于电化学氧化对氯苯酚后表层物相没有发生改变,但其组成元素的含量有所变化.与Ti/SnO2-Sb2O3 和Ti/PbO2 电极相比,Ti/SnO2-Sb2O3/PbO2 电极具有更高的电化学氧化性能.     

碳基复合电极制备和电Fenton降解4-氯酚研究

研究了石墨-PTFE和活性炭-PTFE复合电极的制备工艺,并以4-氯酚模拟废水为对象,比较了石墨-PTFE和活性炭-PTFE复合电极的吸附和电Fenton性能。结果表明,活性炭-PTFE复合电极的吸附性能优于石墨-PTFE复合电极,而石墨-PTFE复合电极的电Fenton处理效果则明显优于活性炭-PTFE复合电极。在实验条件下,电Fenton反应时间为125min时,活性炭-PTFE复合电极的4-氯酚去除率仅为5.79%,而石墨-PTFE复合电极对4-氯酚的去除率高达94.48%。     

Scavenging of Cd through Fe/Mn oxides within natural surface coatings

The dynamics of Cd scavenging from solutions by Fe/Mn oxides in natural surface coatings （NSCs） was investigated under laboratory conditions. Selective extraction methods were employed to estimate the contributions of Fe/Mn oxides, where hydroxylamine hydrochloride （0.01 mol/L NH2OH-HCl ＋ 0.01 mol/L HNO3）, sodium dithionite （0.4 mol/L Na2S2O4） and nitric acid （10% HNO3） were used as extraction reagents. The Cd scavenging was accomplished with developing periods of the NSCs （totally 21 data sets）. The resulting process dynamics fitted well to the Elovich equation, demonstrating that the amount of Cd scavenged was proportional to the increments of Fe/Mn oxides that were accumulated in the NSCs. The amount of Cd bound to Fe oxides （MCdFe） and Mn oxides （MCdMn） could be quantified by solving two equations based on the properties of two extraction reagents. The amount of Cd scavenged by Fe/Mn oxides could also be estimated using MCdFe and MCdMn divided by the total amounts of Fe and Mn oxides in the NSCs, respectively. The results indicated that the Cd scavenging by Fe/Mn oxides was dominated by Fe oxides, with less roles attributed to Mn oxides. The estimated levels of Cd scavenging through Fe and Mn oxides agreed well with those predicted through additive-adsorption and linear-regression models.