动电技术去除城市污泥中镉的研究

采用实际城市污泥为研究对象,通过控制阴极液酸度和添加络合剂,考察了镉的动电过程.结果表明,添加EDTA和柠檬酸不仅改变了动电过程的电流和电渗流,同时对镉的形态分布也产生了明显的影响:存在于移动性较低形态、难以去除的镉被转化为移动性较高的形态,在动电作用下从污泥中移除,从而提高了动电处理的效率,总镉的去除率最高达到70.1%;EDTA和柠檬酸对动电处理的促进作用主要受体系酸度的影响,其中控制阴极pH值为4和8时,总镉的去除率达到66.4%、70.1%、62.3%和66.5%,较pH值为6时去除率提高了2～3倍.比较两种络合剂,EDTA在高pH值条件下对镉的络合能力较强而表现出较高的去除率,而柠檬酸对酸度的适应性相对较强.     

电动修复技术对土壤中镉迁移的影响

以镉含量为200 mg·kg~(-1)的模拟污染土壤为研究对象,使用电动修复技术对土壤中的镉进行去除。实验研究了不同修复电压下电流密度、电解液pH值、土壤中镉含量的变化,并重点研究了修复电压对土壤中镉迁移的影响规律。实验结果表明,通电电压越大,电场强度越强,镉的迁移量越大,电动修复效率越高,当修复电压为50 V时,阴极区域附近镉的迁移量与修复电压为5 V时相同位置镉的迁移量相比可以提高30%,实验结果为重金属污染土壤电动修复过程中镉的迁移量化研究提供了参考。     

阴极液及底物浓度对AFB-MFC同步废水处理及产电性能影响

为了提高厌氧流化床微生物燃料电池（AFB-MFC）的性能，并为双室MFC寻找价廉、易得、无污染的阴极液，在曝气量16～24 L/h、温度（35±2）℃、回流量10.2 L/h、阴极底边距阴极室内底部17.3 cm、外电阻250 Ω、水力停留时间（HRT）14.0～14.9 h以及进水pH 7.81～8.37下，研究了阴极液及底物浓度对系统产电及废水处理性能的影响。结果表明，使用缓冲溶液、阳极室出水和自来水作阴极液时，自来水的产电性能最佳，阴极液种类不影响系统有机基质的去除。以自来水为阴极液时，阴极液pH及电导率随运行时间增加而增加，COD去除率为80.11%～89.29%，输出电压及功率密度开始随运行时间增加而增加，之后稳定在440～452 mV和48.40～51.08 mW/m²之间。增加底物浓度对COD去除率影响不大，而输出电压及功率密度随底物浓度增加而下降；底物COD浓度由3 307.09 mg/L增至9 520 mg/L时，COD去除率在85.77%～94.44%之间，输出电压及功率密度则分别由449 mV和50.40 mW/m²下降至406 mV和41.21 mW/m²。自来水作阴极液可避免二次污染及阴极液对阳极室微生物的影响，并得到高的产电能力。     

剩余污泥中重金属的电动力学修复研究

主要研究了电极材料和电极间距对氢析出电压和电压梯度的影响,以及电极材料、阴极液pH、修复时间对不同形态重金属去除率的影响.实验结果表明,在相同条件下,氢的析出电压和电压梯度受电极材料和电极间距的影响.阳极均为高纯石墨电极,阴极分别为高纯石墨电极、铜电极和铁电极,电极间距在32.5 cm时,高纯石墨为阴极的氢的析出电压最...     

电沉积处理电解锌漂洗废水的实验研究

采用电沉积技术对电解锌漂洗废水进行初步处理，以求达到废水回用和重金属锌的回收。研究了电沉积法处理含锌废水过程中各个影响因素对电沉积效果的影响，并且设计了正交实验。结果表明，极板间距、槽电压、进水pH、极板材料等对二维电沉积处理模拟废水具有显著影响。适宜的电沉积条件是：极板间距20 mm、槽电压5～6 V、阴极板材料为铝板、电沉积时间为30～45 min。     

单室微生物燃料电池处理含铜模拟废水

为了降低废水中重金属的含量,研究了空气阴极单室微生物燃料电池对模拟废水中Cu(Ⅱ)的去除效果。考察了铜的初始浓度、初始pH值和外加电阻等单因子的影响,从Cu(Ⅱ)去除率及电压输出等方面进行考核,确定最佳去除条件:SMFC的最大耐受浓度为12.5 mg·L~(-1),最适Cu(Ⅱ)还原去除的初始pH值为6.0和低电阻500Ω。SMFC出水Cu(Ⅱ)浓度低于0.5 mg·L~(-1),达到《城镇污水处理厂污染物排放标准》(GB18918-2002)中总铜排放标准,拓展了生物电化学系统系统在去除重金属离子废水方面的应用。     

初始pH值对皂苷强化污泥生产短链挥发性脂肪酸的影响

近年来,应用化学表面活性剂强化污泥厌氧生产短链挥发性脂肪酸得到广泛地关注。相较于化学类的表面活性剂,生物表面活性剂具有能够降解,对环境污染小的优点。报道了一种新型的生物表面活性剂皂苷,并用皂苷强化污泥厌氧发酵。实验结果表明,皂苷的最佳投放量为0.2 g·g-1干污泥,相应的最大产酸量为2 149 mg·L~(-1)此外还探究了初始pH值对皂苷强化污泥产酸的影响,实验表明最佳的初始pH为11。机理研究发现初始pH=11能够加速污泥的水解,抑制甲烷产生进而提高了短链挥发性脂肪酸的含量。     

电絮凝处理牛仔布印染废水

用铁分别作为电絮凝反应系统的阴极和阳极,研究电絮凝法对牛仔布印染废水的处理效果。考察了电极电压、反应时间和pH等因素对电絮凝法去除实验所用废水中COD和色度效果的影响。结果表明,电极电压和反应时间是主要的影响因素,pH次之。电极电压24 V,反应时间35 min,pH为7.4时,脱色率可达99%,COD去除率在70%左右,处理效果最佳。因此,电絮凝法可以作为印染废水的预处理工艺,有效降低废水COD和色度。     

吸附分离辅助电渗透脱水过程中污泥的特性

电渗透技术对于城市污水厂污泥的深度脱水是非常有效的,但相对较高的能耗制约了它的广泛应用。为此,针对污泥电渗透脱水过程中阴极排水困难引起能耗高的问题,提出了吸附分离辅助电渗透脱水,同时考察了吸附分离辅助电渗透脱水过程中污泥中水分的运动特点、pH的变化以及离子的迁移规律。结果显示,吸附分离可以极大地提高污泥电渗透脱水的效果。且脱水过程中阳极附近污泥的含水率、pH均迅速减小;阴极附近污泥的含水率稍有减少,但pH却迅速增大;而中间层污泥的含水率及pH均没有发生变化。此外,电渗透脱水技术对于污泥中目标离子的去除非常有效,但同时容易导致非目标离子的去除。     

电-Fenton法处理页岩气压裂返排液

页岩气开发压裂返排液处理是近年的研究热点,本文采用电-Fenton氧化技术对压裂返排液絮凝出水进行深度处理研究,主要考察了H2O2投加量、pH值、电压和反应时间对COD去除效果的影响。通过正交实验和单因素影响实验,确定电-Fenton氧化处理絮凝出水的适宜条件为:H2O2投加量为40 mL·L~(-1)、pH=3、电压6 V和反应时间60 min。在此条件下,出水COD为71.3 mg·L~(-1),COD去除率达到62.5%。实验结果表明化学絮凝—电-Fenton氧化是页岩气压裂返排液达标外排的一种适宜处理工艺。     

Electrokinetic remediation of a Cu-Zn contaminated red soil by controlling the voltage and conditioning catholyte pH

Electrokinetics is an innovative technique for treating heavy metals contaminated soil, especially low pH soils such as the Chinese red soil (Udic Ferrisols). In this paper, a Cu-Zn contaminated red soil is treated by electrokinetics. When the Cu-Zn contaminated red soil was treated without control of catholyte pH during the electrokinetic treatment, the soil pH in the soil sections near cathode after the experiment was high above 6, which resulted in accumulation of large amounts of Cu and Zn in the soil sections with such high pH values. Compared to soil Cu, soil Zn was more efficiently removed from the soil by a controlled electrokinetic method. Application of lactic acid as catholyte pH conditioning solution caused an efficient removal of Cu and Zn from the soil. Increasing the electrolyte strength (salt concentration) of the conditioning solution further increased Cu removal, but did not cause a significant improvement for soil Zn. Soil Cu and Zn fractions after the electrokinetic treatments were analyzed using sequential extraction method, which indicated that Cu and Zn precipitation in the soil section closest to the cathode in the treatments without catholyte pH control limited their removal from the soil column. When the catholyte pH was controlled by lactic acid and CaCl(2), the soil Cu and Zn removal percentage after 554 h running reached 63% and 65%, respectively. Moreover, both the residual soil Cu and Zn concentrations were lower than 100 mg kg(-1), which is adequate and meets the requirement of the Chinese soil environmental quality standards.     

Solid/solution Cu fractionations/speciation of a Cu contaminated soil after pilot-scale electrokinetic remediation and their relationships with soil microbial and enzyme activities

The aim of this study was to investigate the detailed metal speciation/fractionations of a Cu contaminated soil before and after electrokinetic remediation as well as their relationships with the soil microbial and enzyme activities. Significant changes in the exchangeable and adsorbed-Cu fractionations occurred after electrokinetic treatment, while labile soil Cu in the solution had a tendency to decrease from the anode to the cathode, and the soil free Cu²⁺ ions were mainly accumulated in the sections close to the cathode. The results of regression analyses revealed that both the soil Cu speciation in solution phase and the Cu fractionations in solid phase could play important roles in the changes of the soil microbial and enzyme activities. Our findings suggest that the bioavailability of soil heavy metals and their ecotoxicological effects on the soil biota before and after electroremediation can be better understood in terms of their chemical speciation and fractionations.     

鼠李糖脂协助下的土壤中镉电动修复

实验研究了重金属Cd在生物表面活性剂鼠李糖脂协助下的电动修复过程,通过不同方式、不同浓度、不同酸碱度的鼠李糖脂溶液的添加与空白处理对比,探讨了鼠李糖脂协助下电动修复过程中的Cd在土壤介质中的迁移转化和机理,分析了鼠李糖脂溶液作为电动修复添加剂的可行性。结果表明,中等浓度酸性的鼠李糖脂溶液(pH=4.78,浓度为0.5、1和2 g/L)能对土壤中的重金属Cd进行有效的富集,富集量均在初始值的4倍以上,且其可交换态比重均大于42.07%,非常有利于土壤进行二次修复。此外,以pH=4.78,浓度为0.5 g/L的鼠李糖脂溶液作为预处理剂的Ex-08中的重金属Cd并未出现富集现象,但其对重金属的Cd的总去除效率达到了49.27%。表明利用鼠李糖脂溶液作为电动修复添加剂进行土壤重金属修复是可行的。     

组合式水生植物净化系统对Cu、Pb和Cd的去除与生物富集特征

选取再力花、美人蕉、水烛、旱伞草、梭鱼草、慈姑、菖蒲、水葫芦和大薸9种植物作为实验植物,构建成以高效净化重金属污染水体为主要功能的组合式水生植物高效净化系统(人工湿地+生态浮床+水生植物塘3个处理单元串联而成),研究不同处理单元中水生植物对重金属Cu、Pb和Cd的去除能力及富集特征。结果表明,该净化系统经过为期60 d的连续运行,对Cu、Pb和Cd的去除率较为稳定,可分别达到Cu 93.5%~96.1%、Pb 94.5%~95.2%和Cd 95.6%~97.4%,3种重金属出水浓度均可达到GB3838-2002Ⅲ类水排放要求;其中人工湿地单元对重金属去除贡献率最高,Cu、Pb和Cd分别为54.15%、33.61%和44.84%,其次为生态浮床处理单元,Cu、Pb和Cd的去除贡献率分别为38.61%、51.42%和38.56%,而水生植物塘主要起到深度处理作用,对Cu、Pb和Cd的去除贡献率分别为7.24%、14.97%和16.6%。9种植物在系统运行期间,生长状况良好,且重金属累积量较高,尤其是生物塘系统中的水葫芦和大薸,实验期间其重金属生物富集系数(BCF)均在200以上。所选植物不同部位对3种重金属的吸收富集能力均表现为根最强。     

可渗透反应复合电极法对土壤重金属的电动去除

将零价铁(Fe0)、沸石等活性材料附着在电极上形成可渗透反应层并构成可渗透反应复合电极,采用不同的复合电极对Cd2+、Ni 2+、Pb2+和Cu2+等4种阳离子型重金属污染土壤进行了电动力学修复。研究了不同可渗透反应复合电极对土壤pH的控制效果以及对重金属的去除作用,分析了迁移到复合电极中的重金属形态变化。结果表明,复合电极中添加酸、碱性沸石并适时更换,可有效中和、截留阴阳极电解产生的OH-和H+,避免或减缓土壤酸碱迁移带的形成,防止重金属离子的过早沉淀及土壤过度酸化,极大提高了重金属的去除率。复合电极中Fe0可将迁移进来的重金属离子进行还原稳定,实现重金属污染物的捕获与固定,与迁移到沸石复合电极中的4种重金属不稳定态相比,"Fe0+沸石"复合电极中重金属不稳定态分别下降了61.4、60.5、61.4、57.1百分点。结果还显示,阴极采用"Fe0+沸石"复合电极并适时进行更换,施加1.5V/cm的直流电压修复10d后,土壤中Cd、Ni、Pb、Cu的总去除率分别为44.5%、41.5%、33.5%和36.7%,且进一步延长修复时间和持续更换电极可获得更为理想的修复效果。     

EDTA强化电动力学修复重金属复合污染土壤

在自制的电动力学装置中,研究多种重金属复合污染土壤的电动力学修复,通过在阴极添加络合剂EDTA来提高修复效率。实验结果表明,EDTA的引入提高了修复过程中的电流值,且EDTA与重金属的络合提高了污染物向电极液的迁移效率,从而强化了电动力学修复效果。在设定的浓度(0、0.01、0.02、0.05和0.1 mol/L)中,0.1 mol/L的EDTA具有最佳的修复效率。在此实验条件下,污染土壤中的总铜、总铅和总镉的去除率分别为90.2%、68.1%和95.1%。电动力学修复后,对土壤重金属进行化学形态分析,发现电动力学修复显著改变了土壤重金属存在形态,修复后土壤中的铜、铅、镉主要以较稳定的有机态和残余态形式存在,显著降低了对周边生物和环境的毒害。     

Electrokinetic remediation of a Cu contaminated red soil by conditioning catholyte pH with different enhancing chemical reagents

The effect of enhancement reagents on the efficiency of electrokinetic remediation of Cu contaminated red soil is evaluated. The enhancement agents were a mix of organic acids, including lactic acid+NaOH, HAc-NaAc and HAc-NaAc+EDTA. The soil was prepared to an initial Cu concentration of 438 mgkg(-1) by incubating the soil with CuSO4 solution in a flooded condition for 1 month. Sequential extraction showed that Cu was partitioned in the soil as follows: 195 mgkg(-1) as water soluble and exchangeable, 71 mgkg(-1) as carbonate bound and 105 mgkg(-1) as Fe and Mn oxides. The results indicate that neutralizing the catholyte pH maintains a lower soil pH compared to that without electrokinetic treatment. The electric currents varied depending upon the conditioning solutions and increased with an increasing applied voltage potential. The electroosmotic flow rate changed significantly when different conditioning enhancing reagents were used. It was observed that lactic acid+NaOH treatments resulted in higher soil electric conductivities than HAc-NaAc and HAc-NaAc+EDTA treatments. Ultimately, enhancement by lactic acid+NaOH resulted in highest removal efficiency (81% Cu removal) from the red soil. The presence of EDTA did not enhance Cu removal efficiencies from the red soil, because EDTA complexed with Cu to form negatively charge complexes, which slowly migrated toward the anode chamber retarding Cu2+ transport towards the cathode.     

Comparison of electrokinetic soil remediation methods using one fixed anode and approaching anodes

During the cation exchange membrane (CEM) enhanced electrokinetic (EK) soil remediation, the nearer to the anode, the higher are the H+ concentrations and the redox potentials. As both low pH and high redox potential are helpful to speed-up Cd electro-migration, soils near the anode can be quickly remedied. Usually EK process is operated with one fixed anode (FA). A novel CEM enhanced EK method with approaching anodes (AAs) is proposed to accelerate electro-migration effect. Several mesh Ti/Ru anodes were inserted as AAs in the treated soil. They were switched in turn from the anode towards the cathode. Thus high H+ ions concentrations and high redox potentials quickly migrate to the cathode. Consequently, soil remediation is accelerated and nearly 44% of energy and 40% of time can be saved. The mechanism of Cd electro-migration behavior in soils during CEM enhanced EK is described as the elution in an electrokinetically driven chromatogram.     

几种模拟处理方式污泥淋出液重金属与养分特征

为了减少城市污泥重金属对农田的污染,更好地实现污泥农业资源化利用,通过盆栽实验研究不同处理(对照、黑网、附Fe黑网、附Fe黑网+K2SO4及附Fe黑网+玉米)对城市污泥淋出液重金属和养分含量等的影响。结果表明,黑网可降低污泥淋出液的Zn﹑Cd总量,且没有减少污泥淋出液中氮、磷和钾的总量。Fe(OH)3可使淋出液中Zn总量降低,但同时也显著减少了淋出液中的磷总量。K2SO4可降低淋出液中的Cu总量,且促进Fe结合磷的释放。玉米的种植可使污泥的总重降低,同时玉米籽粒和茎叶重金属含量达到饲料标准。综合来看,任何处理每次淋出液的Cu、Zn、Pb、Cd浓度均符合农田灌溉水标准,淋出液氮、磷、钾量占原污泥中氮、磷、钾总量的比例(0.98%～9.88%)远远大于重金属元素(Cu,Zn,Pb,Cd)占原污泥对应重金属总量的比例(0.04%～0.41%),污泥淋出液作为农田灌溉水进行肥水利用将是污泥农业资源化利用的适合途径,同时黑网+玉米处理可能是较理想的污泥综合处理利用方式。     

A two-stage process using electrokinetic remediation and electrochemical degradation for treating benzo[a]pyrene spiked kaolin

An innovative process that combines soil electrokinetic remediation and liquid electrochemical oxidation for the degradation of organic compounds present in a polluted soil was developed and evaluated by using benzo[a]pyrene spiked kaolin. In order to increase benzo[a]pyrene solubility during electrokinetic treatment, the addition of a co-solvent or surfactant, such as ethanol or Brij 35, as flushing solution was tested. The research carried out demonstrated the influence of the desorption agent employed on benzo[a]pyrene remediation from the kaolin matrix. Thus, if the flushing solution was ethanol at 40%, there was no presence of contaminant in either chamber. On the contrary, when a solution of surfactant Brij 35 was used, benzo[a]pyrene was transported towards the cathode chamber, where it was collected. Moreover, the extent of this recovery depends on the pH profile on the soil. When no pH control was used, around 17% of initial contaminant was detected in the cathode chamber; however, when pH control was applied, the recovery of benzo[a]pyrene could be higher than 76%, when the pH control in the anode chamber was set at 7.0.In order to obtain the total degradation of mobilised benzo[a]pyrene from the contaminated soil, the liquid collected by electrokinetic remediation was oxidised by electrochemical treatment. This oxidation was accomplished via an electrochemical cell with a working volume of 0.4 L, and graphite as electrode material. The benzo[a]pyrene was almost totally degraded in 1 d, reaching a degradation of about 73% in 16 h.