电动修复不同形态铬污染土壤的研究

研究了土壤中铬的价态对电动修复效率的影响以及电动修复前后土壤中铬形态的变化.结果表明,电动修复对于土壤中1 000 mg Cr(Ⅵ)/kg的去除效果明显,总铬去除率达59.7%;而对1 000 mg Cr(Ⅲ)/kg的去除效率较低,仅为6.2%;Cr(Ⅲ)和Cr(Ⅵ)(各500 mg/kg)同时污染的土壤,铬的去除率介于中间,为18.7%.电动修复前后,土壤中铬的形态也发生了明显的变化.其中,电动修复对土壤中Cr(Ⅵ)的提取形态影响最大,而对Cr(Ⅲ)提取形态并无太大的影响.总体上,电动修复后对于生物有效的弱酸可提取态铬的浓度都保持在较低水平,预期铬的环境风险(物理流动性和生态风险)将大大降低.     

复合淋洗剂柱淋洗法修复工业废弃地铬污染土壤

为了更好地修复铬污染土壤,以盐酸、柠檬酸为初始淋洗剂,配合去离子水、石灰水、氯化钙、碳酸钠和磷酸钠,制定了20种复合淋洗剂的淋洗方案对某工业废弃地铬污染土壤进行柱淋洗实验,研究复合淋洗剂对土壤pH、总铬和Cr(Ⅵ)去除效果及对各形态铬变化的影响。结果表明:(1)各淋洗方案对土壤总铬和Cr(Ⅵ)的去除量分别为197.4~1 671.6、113.2~316.8mg/kg,其中初始淋洗剂盐酸、柠檬酸结合使用对总铬有较好的去除效果。(2)石灰水和磷酸钠可以将淋洗后的土壤pH调至接近中性并固定尚未淋洗出的Cr(Ⅵ)。(3)当0.2mol/L柠檬酸、0.1mol/L盐酸、0.2mol/L盐酸、1%(质量分数)石灰水用量分别为2、2、1、2mL/g进行淋洗时,土壤pH为7.37,总铬和Cr(Ⅵ)去除量分别为1 659.8、316.8mg/kg,去除率分别为34.6%、72.7%,水溶态铬、可交换态铬和碳酸盐态铬已被大量淋出,有机态铬与残渣态铬占比较其他淋洗方案低,为最佳淋洗方案。     

高浓度铬污染土壤水浸泡与电动修复联合处理实验

对含铬量为2 142 mg/kg的铬污染土壤首先使用蒸馏水进行6轮浸泡试验,然后再进行电动修试验。土壤经过浸泡、通电24 h和72 h处理后总铬的去除率分别为:47%、61%和70%,表明预浸泡可以显著降低电动修复的负荷从而降低整个土壤修复费用。电动修复过程中对土壤两端的温度进行了测量以间接反映土壤电阻的分布和变化情况。结果显示土壤电阻逐渐上升,从阴极端开始逐渐过渡到阳极端,60 h之后达到最高值并保持稳定。电动修复的电流效率随土壤中铬浓度的降低而下降。此外,浸泡和电动修复均导致整个土壤和各断面铬浓度分布不均匀性增大。     

生物炭-微生物复合材料修复Cr(Ⅵ)污染土壤条件优化及促生效果

生物炭和微生物在改善Cr(Ⅵ)污染土壤质量方面得到了广泛的应用,而以生物炭-微生物制备的复合材料(BC-MT)在Cr(Ⅵ)污染土壤修复中的促生效果鲜见报道。以玉米秸秆生物炭为载体吸附铬还原菌——藤黄微球菌(Micrococcus luteus)制备BC-MT,综合考察了BC-MT修复Cr(Ⅵ)污染土壤最佳条件及促生效果。结果表明:藤黄微球菌能成功附着在生物炭上,BC-MT对Cr(Ⅵ)污染土壤修复效果显著,在BC-MT投加量3%(质量分数,下同)、氮源投加量10g/kg、土壤含水率14%的条件下,修复25d,Cr(Ⅵ)去除率为64.35%,可提取态铬从27.01mg/L降至7.72mg/L。在3%BC-MT作用下,植物生长12周后地上、地下部分总铬含量分别降低了65.15%、49.76%,Cr(Ⅵ)分别降低了94.11%、87.74%,植物株高增加了17.7cm,生物量(以干重计)增加了132mg,叶绿素增加了4.65mg/g,可溶性糖增加了1.69mg/g。由此可见,BC-MT不但能有效降低土壤Cr(Ⅵ)含量,而且促生效果显著,具有广阔的应用价值。     

电动-氧化修复条件对土壤中多环芳烃和重金属去除的影响探索

电动-氧化修复可同时去除污染土壤中的重金属和有机物,但需要控制合适的条件,因此研究了电动-氧化修复的条件对土壤中多环芳烃(PAHs)和重金属去除的影响。结果表明,阴极安装阳离子交换膜可避免氧化剂与阴极直接接触,提高氧化剂在土壤中的输送效率,PAHs总平均去除率达82.8%,同时可维持土壤pH在中性范围,土壤电导率(EC)变化较小,但对重金属的去除率也较小;控制阴极液pH为酸性,PAHs总平均去除率可达96.2%,对重金属也有一定的去除作用,然而会改变土壤pH和EC。相对来说,阴极安装阳离子交换膜是一种比较可行的电动-氧化修复处理条件,PAHs去除率高,对土壤性质的影响小,但对重金属去除率不高。维持土壤基本性质的基础上,如何同时高效去除PAHs和重金属的条件还需进一步研究。     

电化学联合H_2O_2氧化淋洗修复典型化工厂遗留地铬污染土壤

选取的济南某化工厂遗留地土壤主体为褐土类,年均降水量在685 mm左右,铬污染场地面积约34万m2,土量约105.4万m3。为筛选出最佳氧化条件,研究了4个厂区铬污染土壤的理化性质和污染状况,探讨了通电时间、通电电压、氧化剂质量分数、土液比和pH对Cr(Ⅲ)转化成Cr(Ⅵ)比率和总铬去除率的影响。结果表明:4个厂区土壤酸碱性不同;万吨铬盐生产车间和北部厂区有机质含量较高,其他2个厂区较低;总铬含量在863.3~14 403.8 mg·kg-1之间,均严重超出国家标准;铬污染活性指数I在0.007 8~0.292 9之间,铬污染活性指数均较低;最佳通电时间选择为20 min,通电电压为10 V,H2O2质量分数为1%,土液比为2:3,pH为8。经修复,4个厂区剩余总铬浓度分别为363.68、258.09、6 938.31和495.45 mg·kg-1,最大总铬去除率分别可达到87.59%、73.95%、51.83%和42.61%,其中万吨铬盐生产车间土壤中总铬残留值可达到国家土壤环境质量二级标准(GB 15618-2008)修订稿中的居住用地标准,铬盐生产车间和北部厂区可达到修订稿中的商业用地标准。     

废铁屑-改性粉煤灰联用处理铬渣渗滤液

针对铬渣严重污染环境问题,以"以废治废"为研究目标,采用室内静态实验方法,进行废铁屑-改性粉煤灰联用处理铬渣渗滤液中Cr(Ⅵ)和总铬实验研究。实验结果表明,废铁屑与聚合氯化铝改性粉煤灰联用处理Cr(Ⅵ)和总铬效果优于单独采用其中一种物质;处理Cr(Ⅵ)浓度208 mg/L、总铬浓度260 mg/L的200 m L高浓度含铬废水最佳反应条件为:反应时间30 min,总投加量40 g,配比为1∶1,pH值4.1,对应Cr(Ⅵ)去除率99.93%,总铬去除率99.72%。处理后水质满足《污水综合排放标准》(GB 8978-1996)要求。     

米糠生物质解毒含铬(Ⅵ)水溶液的研究

农林生物质是一种成本低、环境友好的重金属废水处理材料,也是受重金属污染环境的修复材料之一.实验讨论了初始pH值、米糠用量、吸附时间对含铬(Ⅵ)水溶液解毒的影响.结果表明,米糠对Cr(Ⅵ)存在吸附作用,同时也有解毒还原能力.100 mL浓度为100 mg/L的含铬溶液,在初始pH为2、米糠用量为3 g、吸附-反应平衡时间7 h的条件下,生物质吸附去除溶液中的铬为14.4%,而原溶液中Cr(Ⅵ)解毒了57.2%,米糠生物质吸附总铬的能力为0.48 mg Cr/g(生物质).米糠生物质有潜在的吸附铬和修复受铬污染环境的利用价值.     

铁系物还原稳定化技术修复铬污染土壤应用研究

铁系物还原与稳定化是修复铬(Cr)污染土壤的重要手段。采用硫化亚铁(FeS)、硫酸亚铁(FeSO₄)、四氧化三铁(Fe₃O₄)和纳米零价铁(nZVI)4种铁系物对Cr(Ⅵ)污染土壤进行修复，优化修复条件，并进一步联用3种稳定剂(石英砂、高岭土和石灰石)对Cr(Ⅵ)污染土壤进行修复。结果表明，4种铁系物对土壤Cr(Ⅵ)的还原效果为FeSO₄>nZVI>Fe₃O₄>FeS,3种稳定剂对土壤总Cr和Cr(Ⅵ)的稳定化效果为高岭土>石灰石>石英砂。其中，nZVI-石英砂和nZVI-高岭土联用对土壤Cr(Ⅵ)的还原率超过99%,修复后，土壤中可交换态和碳酸盐结合态的Cr含量减少，残渣态Cr含量增加。     

生物铁修复Cr(Ⅵ)污染土壤的性能及机理

以活性污泥与生物铁作为修复剂,对比时间、pH、污泥投加量、Cr(VI)初始浓度对活性污泥、生物铁去除土壤中Cr(VI)的影响;考察生物铁对土壤中Cr(VI)的还原率;采用SEM、XRD、XPS对生物铁修复前后的Cr(VI)污染土壤进行表征分析。实验结果表明:在土壤中,生物铁对Cr(VI)的修复效果优于活性污泥,当pH为6.0,Cr(VI)初始浓度为300 mg·kg~(-1),生物铁和活性污泥的投加量均为19.57 mg·g~(-1),修复时间为45 d时,土壤中Cr(VI)经活性污泥与生物铁修复后浓度分别为31.42、19.69 mg·kg~(-1),去除率分别为89.52%、94.12%。生物铁修复土壤Cr(VI)以还原作用为主,吸附为辅。Cr(VI)污染土壤被生物铁修复后出现了FeOOH、Fe_3O_4以及Fe_3O_4与FeCr2O4的混合物,部分Cr(VI)被还原为Cr(III),铁被氧化为Fe~(2+)、Fe~(3+)。     

Electro-migration of heavy metals in an aged electroplating contaminated soil affected by the coexisting hexavalent chromium

Cr(VI) was often reported to oxidize soil organic matter at acidic environments due to its high ORP, probably thus changing cationic metal species bound to soil organic matter, and influencing their electro-migration patterns. However, such an effect on the electro-migration was not confirmed in most previous studies. Therefore, this study applied a fixed voltage direct current field on an aged electroplating contaminated clayed soil, with a special interest in the direct or indirect influence of Cr(VI) on the electro-migration of other coexisting metals. After 353 h electrokinetic process, 81% of Zn, 53% of Ni and 22% of Cu in the original soil were electro-migrated into the electrolyte, and most of the remaining concentrated near the cathode. The Cr(VI) oxidized some soil organic matter along its migration pathway, with a pronounced reaction occurred near the anode at low pHs. The resulting Cr(III) reversed its original movement, and migrated towards the cathode, leading to the occurrence of a second Cr concentration peak in the soil. Metal species analyses showed that the amount of metals bound to soil organic matter significantly decreased, while a substantial increase in the Cr species bound to Fe/Mn (hydro-)oxides was observed, suggesting an enhancement of cationic metal electro-migration by the reduction of Cr(VI) into Cr(III). However, the Cr(VI) may form some stable lead chromate precipitates, and in turn demobilize Pb in the soil, as the results showed a low Pb removal and an increase in its acid-extractable and residual fractions after electrokinetic remediation.     

Transient behavior of heavy metals in soils during electrokinetic remediation

This paper presents a systematic bench-scale laboratory study performed to assess the transient behavior of chromium, nickel, and cadmium in different soils during electrokinetic remediation. A series of laboratory electrokinetic experiments was conducted using two different clayey soils, kaolin and glacial till. For each type of soil, four electrokinetic experiments with 1, 2, 4, and 10 d of treatment time were performed. In all tests, the contaminants were Cr(VI), Ni(II), and Cd(II) combined in the soil. A geochemical assessment was performed using the geochemical model MINEQL(+) to determine the partitioning of the heavy metals in soils as precipitated, adsorbed, and aqueous forms. Results showed that in kaolin, the extent of Ni(II) and Cd(II) migration towards the cathode increased as the treatment time increased. Unlike kaolin, in glacial till treatment time had no effect on nickel and cadmium migration because of its high buffering capacity. In both kaolin and glacial till, the extent of Cr(VI) migration towards the anode increased as the treatment time increased. However, Cr(VI) migration was higher in glacial till as compared to kaolin because of the high pH conditions that existed in glacial till. In all tests, some Cr(VI) was reduced to Cr(III), and the Cr(VI) reduction rate to Cr(III) as well as the Cr(III) migration were significantly affected by the treatment time. Overall, this study showed that the electroosmotic flow as well as the direction and extent of contaminant migration and removal depend on the polarity of the contaminant, the type of soil, and the treatment duration.     

Remediation of chromium-contaminated soil by electrokinetics and electrokinetics coupled with CaAl-LDH permeable reaction barrier

Environmental Science and Pollution Research - The remediation of Cr(VI)-contaminated soil was investigated by electrokinetic (EK) and permeable-reactive-barrier assisted electrokinetic (EK-PRB)....     

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。     

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。     

Leaching behavior of Cr(III) in stabilized/solidified soil

The leaching behavior of chromium was studied using batch leaching tests, surface complexation modeling and X-ray absorption near edge structure (XANES) spectroscopy. A contaminated soil sample containing 1330 mg-Cr kg(-1) and 25600 mg-Fe kg(-1) of dry soil was stabilized/solidified (S/S) with 10% cement, 25% cement, 10% lime and a mixture of 20% flyash and 5% lime. The XANES analysis showed that Cr(III) was the only Cr species in untreated soil and S/S-treated samples. The leachate Cr concentration determined using the toxicity characteristic leaching procedure (TCLP) was reduced from 5.18 mg l(-1) for untreated soil to 0.84 mg l(-1) for the sample treated with 25% cement. The Cr leachability in untreated and treated soil samples decreased dramatically as the pH increased from 3 to 5, remained at similar levels in the pH range between 5 and 10.5, and further decreased at pH>10.5. Modeling results indicated that the release of Cr(III) was controlled by adsorption on iron oxides at pH<10.5, and by precipitation of Ca(2)Cr(2)O(5).6H(2)O at pH>10.5.     

高原地区铬渣污染场地污染特性研究

在我国高原地区某铬渣污染场地进行钻孔取样,分析场地工程地质特性,对场地铬的污染状况及空间分布特征进行研究。结果表明:场地地质结构较单一,地下水丰富,土质的渗透性强,渗透系数在1.78×10-3~0.243 cm/s之间;场地铬污染严重,总铬与六价铬的浓度最大值分别为22 485.6 mg/kg和7 495.2 mg/kg,地下水中六价铬的浓度最大值为107.2 mg/L;通过剖面铬浓度分析:铬在纵向上浓度分布受土壤质地的影响,均呈现表层4 m浓度较高,4 m以下浓度较低且变化较小的规律。由Kriging插值法绘的铬浓度分布等值线图可清晰看出场地表层土表现出向沟谷位置迁移趋势,地下水中残留的铬向地下水流场方向迁移。     

Spatial variability of arsenic and chromium in the soil water at a former wood preserving site

Contamination of industrial sites by wood preservatives such as chromated copper arsenate (CCA) may pose a serious threat to groundwater quality. The objective of this study was to characterise the spatial variability of As and Cr concentrations in the solid phase and in the soil water at a former wood impregnation plant and to reveal the fundamental transport processes. The soil was sampled down to a depth of 2m. The soil water was extracted in situ from the vadose zone over a period of 10 months at depths of 1 and 1.5m, using large horizontally installed suction tubes. Groundwater was sampled from a depth of 4.5m. Results showed that arsenic and chromium had accumulated in the upper region of the profile and exhibited a high spatial variability (As: 21-621 mg kg(-1); Cr: 74-2872 mg kg(-1)). Concentrations in the soil water were high (mean As 167 microg L(-1); Cr: 62 microg L(-1)) and also showed a distinct spatial variability, covering concentration ranges up to three orders of magnitude. The variability was caused by the severe water-repellency of the surface soil, induced by the concurrent application of creosote wood preservatives, which leads to strong preferential flow as evident from a dye experiment. In contrast to soil water concentrations, only low As concentrations (<12 microg L(-1)) were detected in the groundwater. High Cr concentrations in the groundwater (approx. 300 microg L(-1)), however, illustrated the pronounced mobility of chromium. Our study shows that at sites with a heterogeneous flow system in the vadose zone a disparity between flux-averaged and volume-averaged concentrations may occur, and sampling of soil water might not be adequate for assessing groundwater concentrations. In these cases long-term monitoring of the groundwater appears to be the best strategy for a groundwater risk assessment.     

Removal of organic contaminants from soils by an electrokinetic process: the case of atrazine. Experimental and modeling

The atrazine behaviour in soils when submitted to an electric field was studied and the applicability of the electrokinetic process in atrazine soil remediation was evaluated. Two polluted soils were used, respectively with and without atrazine residues, being the last one spiked. Four electrokinetic experiments were carried out at a laboratory scale. Determination of atrazine residues were performed by enzyme-linked immunosorbent assay (ELISA). The results show that the electrokinetic process is able to remove efficiently atrazine in soil solution, mainly towards the anode compartment: Estimations show that 30-50% of its initial amount is removed from the soil within the first 24h. A one-dimensional model is developed for simulating the electrokinetic treatment of a saturated soil containing atrazine. The movement of atrazine is modelized taking into account the diffusion transport resulting from atrazine concentration gradients and the reversed electro-osmotic flow at acidic soil pH.     

Improvement in electrokinetic remediation of heavy metal spiked kaolin with the polarity exchange technique

In the electrokinetic treatment of heavy metal polluted soil, an alkaline environment is generated at the cathode side. It provokes the precipitation of metal ions as hydroxides into the soil and diminishes the capability of the electroremediation to clean the polluted site. In this work the "polarity exchange" technique is presented as a simple way to avoid the negative effect of OH(-) on metal transportation. This technique lies in the operation during short time intervals at inverted polarity, so that the generation of H+ ions from the oxidation of water neutralize in the alkaline zone where the metal is precipitated, favouring its dissolution. Once the metals are redissolved, the polarity is set to the original position to transport them to the desired direction. Kaolin clay contaminated with Mn was used to test the feasibility of the polarity exchange technique. The application of the "conventional technique" dealt with a removal of 14% of the initial Mn in 7.6d. For a similar treatment time the polarity exchange technique resulted in 72% of removed Mn. Successive polarity exchanges will yield with a complete decontamination of the soil with a moderate increment in the electric power consumption.