电解液对直流电场处理石油污染土壤的影响

直流电场处理石油污染土壤技术是一种发展中的土壤修复技术,有诸多优点。在该修复过程中,电解液的成分、电解液p H值控制对通过土壤的电流、土壤含水率、土壤含油率产生了影响。直流电场处理中通过土壤的电流与电解液成分、电解液p H值、土壤电导率和土壤湿度等因素密切相关。采用直流电场处理石油污染土壤效果明显,最低石油去除率达到73.6%。当电解液为0.1 mol/L的Na2CO3时,通过调节p H值,可使通过土壤的电流达到1.6 A、土壤电导率达到0.9S/m。处理后阴极、阳极和中间3个位置的土壤含油率分别从0.4672%降到0.0696%、0.0684%、0.0625%,石油去除率达到了85.1%。     

表面活性剂清洗处理重度石油污染土壤

为了优化表面活性剂清洗处理重度石油污染土壤的方法和具体洗脱条件参数,采集山东省东营市胜利油田污染土壤,研究了阴离子-非离子混合表面活性剂对该土壤中石油类污染物的去除效果。应用化学热洗原理,主要考查了表面活性剂配比、投加量、清洗温度及清洗助剂对去除效果的影响。实验得到的清洗处理最佳条件为：使用LAS与TX-100质量比为8∶2的组合表面活性剂,总表面活性剂浓度为3 g/L,助剂硅酸钠浓度为5 g/L,75℃条件下搅拌1 h。清洗后土壤含油量从20%下降到4.6%,去除率达到76.9%。废水回用实验表明,清洗处理的废水对土壤中石油烃类物质仍有一定的去除效果。废水回用比从30%到100%时,对土壤中石油烃的去除率都可达到55%以上。对废水进行二次回用时仍能去除18.8%的污染物。     

热化学清洗法洗涤油泥-回收石油的工艺条件研究

以辽河油田落地油泥为样品,采用热化学清洗法洗涤油泥,净化土壤,回收石油,并获取工程所需的必要参数.通过筛选、复配,确定十二烷基苯磺酸钠(LAS):NazSiO3=1:2(质量比)为最佳清洗剂配比.考察了清洗温度、清洗液pH、液固比(即清洗剂与落地油泥的质量比)和清洗剂投加量等因素对清洗效率的影响,通过正交实验优化工艺参数,实验表明,当清洗时间为30min、清洗温度为75℃、搅拌器转速为200 r/min、液固比为8:1、清洗液pH为11、LAS Na2SiO3投加量为2.8 g/L时,含油率为21.2%(质量分数)的落地油泥样品经一级清洗,油泥残油率降为0.8%(质量分数,下同);经二级清洗,油泥残油率降为0.3%.清洗后,石油浮于水面,无明显乳化,易于分离.     

木质素盐在原油污染土壤清洗中的应用

木质素磺酸盐价格低廉,容易获得,若将其作为洗油剂中的牺牲剂,可较大幅度地降低洗油成本.以华北油田原油、华北平原典型表层土壤为模拟原料,配制了石油污染土壤,探讨木质素磺酸铵和木质素磺酸钠的洗油性能,以及木质素磺酸盐与壬基酚聚氧乙烯醚、曲拉通和平平加的复配效果.实验以碳酸钠和硅酸钠为助剂,经反复实验筛选,确定了4组最佳洗油剂配方:(Ⅰ)6(曲拉通):6(平平加):8(木素钠):40(硅酸钠):40(碳酸钠);(Ⅱ)6(曲拉通):6(壬酚聚醚):8(木素钠):35(硅酸钠):45(碳酸钠);(Ⅲ)9(曲拉通):3(壬酚聚醚):8(木素钠):50(硅酸钠):30(碳酸钠);(Ⅳ)6(曲拉通):6(壬酚聚醚):3(木素铵):5(木素钠):35(硅酸钠):45(碳酸钠).以此配方为基础,利用正交实验设计对搅拌温度、时间、固液比和加药浓度等工艺条件进行了优化.结果表明:当搅拌温度75℃、搅拌时间50 min、固液比1:15、加药总浓度为0.3g/L时,洗油率可达92.25%.清洗后污油无明显乳化现象,且浮于液面,只须简单刮油即可回收.     

木质素盐在原油污染土壤清洗中的应用

木质素磺酸盐价格低廉,容易获得,若将其作为洗油剂中的牺牲剂,可较大幅度地降低洗油成本.以华北油田原油、华北平原典型表层土壤为模拟原料,配制了石油污染土壤,探讨木质素磺酸铵和木质素磺酸钠的洗油性能,以及木质素磺酸盐与壬基酚聚氧乙烯醚、曲拉通和平平加的复配效果.实验以碳酸钠和硅酸钠为助剂,经反复实验筛选,确定了4组最佳洗油剂配方：（Ⅰ）6（曲拉通）：6（平平加）：8（木素钠）：40（硅酸钠）：40（碳酸钠）;（Ⅱ）6（曲拉通）：6（壬酚聚醚）：8（木素钠）：35（硅酸钠）：45（碳酸钠）;（Ⅲ）9（曲拉通）：3（壬酚聚醚）：8（木素钠）：50（硅酸钠）：30（碳酸钠）;（Ⅳ）6（曲拉通）：6（壬酚聚醚）：3（木素铵）：5（木素钠）：35（硅酸钠）：45（碳酸钠）.以此配方为基础,利用正交实验设计对搅拌温度、时间、固液比和加药浓度等工艺条件进行了优化.结果表明：当搅拌温度75℃、搅拌时间50 min、固液比1：15、加药总浓度为0.3g/L时,洗油率可达92.25%.清洗后污油无明显乳化现象,且浮于液面,只须简单刮油即可回收.     

微波修复石油污染土壤升温特性影响因素的实验研究

实验研究了微波功率、土壤受污染程度和各种吸波介质对微波修复石油污染土壤升温特性的影响,所用的吸波介质有水、颗粒活性炭、铝、镍、三氧化二钴、三氧化二铬和氧化锡.实验中以氮气为保护气微波辐照各种石油污染土壤样品,测量样品的升温特性.实验结果表明:(1)随着微波加热功率的增加,石油污染土壤的升温速率和最高温度都增大,功率从4...     

石油污染土壤生物修复菌Z1a-B的分离鉴定与调控效应研究

从山东东营胜利油田附近的石油污染土壤中分离筛选得到一株高效石油降解菌Z1a-B,通过菌落形态及显微镜个体形态观察对其初步鉴定到属,并采用气相色谱/质谱(GC/MS)法分析了Z1a-B的石油降解性能,采用投加石油降解菌、调节土壤N、P含量和优化环境因素等措施,进行了为期60d的石油污染土壤室外自然堆制生物修复实验。结果表明,Z1a-B为链霉菌属白孢类群,其摇瓶培养的石油降解率为66.4%;Z1a-B有着很宽的烷烃降解谱;N、P最佳的添加量组合为KNO32.50g/kg、K2HPO40.35g/kg,即N/P(质量比)为5.57:1.00,此时的石油降解率达63.5%,土壤脱氢酶活性达最高值,为2.99μL/g;石油降解的最佳环境条件为:将石油质量分数为3.3%的100g土样调节pH至8.5后,装入容积为300mL的锥形瓶中灭菌,再接种孢子密度为2.7×108个/mL的菌剂5.5mL,于28℃下进行生物降解,在此条件下的石油降解率可达76.5%;土壤脱氢酶活性的测定结果可以作为检验石油污染土壤生物修复效果的重要指示指标之一;室外自然堆制生物修复实验中,添加菌剂、锯末、秸秆以及N、P后,石油降解率可达69.9%,总体来说,室外自然堆制生物修复是一种投资少、见效快、治理效果较好的石油污染土壤治理方法。     

油浸泥土热脱附修复小试实验条件的探索

针对油浸泥土中石油烃去除机制不清的问题,利用自制热解炉小试装置,研究了不同条件下油浸泥土中石油烃的处理效果,通过调节加热温度、时间、初始含油率和初始含水率等参数,模拟油浸泥土热脱附过程。结果表明:利用小试装置,当初始含油率为11.3%、初始含水率为20%时,热脱附温度300°C、热脱附时间4 h为最佳处理工艺,处理后油浸泥土中的含油率可降低至0.7%,远低于《油气田含油污泥综合利用污染控制要求》(DB 65/T 3998-2017)中2%的修复标准,石油烃的去除率可达到93.8%;在常见油浸泥土含水率20%及最佳处理工艺下,随着初始含油率的升高,热脱附处理后的固相含油率逐渐升高,但石油烃去除率基本保持不变。适中的油浸泥土含水率有利于热脱附处理,最佳初始含水率为10%～20%。     

石油降解菌群的筛选、构建及其降解特性研究

为了构建高效石油降解混合菌群,从潜江某油田采集8个石油污染土样(分别记为S1~S8)和2个石油污染水样(分别记为W3、W4),以石油为唯一碳源进行富集驯化培养;采用外观评分、石油降解率、石油3组分降解率、饱和烃中正构烷烃色谱分析等方法筛选石油降解优势菌群,构建石油降解混合菌群;采用正交试验研究混合菌群最佳降解条件。结果表明,富集的10个石油降解菌群中S3、S4、S5、S6、S8为优势菌群,培养30d后的石油降解率分别为21.67%、22.34%、27.23%、20.46%、19.99%;菌群W3、W4对石油乳化效果较好;混合菌群M3(S3+S4+S5+S8+W3+W4)为石油降解优势混合菌群,其最佳降解条件为35℃、pH7.60、含油率1.70%,在最佳条件下培养30d后,混合菌群M3对石油降解率达30.71%,比最优菌群S5的石油降解率提高了12.78%。     

微波催化氧化修复技术处理有机氯污染土壤

采用微波催化氧化修复技术处理常州某农药厂有机氯农药污染场地和南通某化工厂有机氯污染场地土壤,考察不同参数条件下实验装置对污染土壤的处理效能。结果表明,在微波功率18kW、微波辐射时间20min、土壤处理量400kg/h、土壤含水率15%、活性炭添加量0.03kg/kg的最佳条件下,实验装置运行稳定,有机氯农药污染土壤中氯丹去除率可达70%左右;有机氯污染土壤中邻二氯苯、石油烃总量、1,2-二氯乙烷、苯酚去除率分别可达到99.98%、91.29%、98.52%、74.74%。研发的污染土壤微波催化氧化修复技术及实验装置对有机氯污染土壤的修复具有一定的普适性。     

Crude oil contaminated soil washing in air sparging assisted stirred tank reactor using biosurfactants

This study investigated the removal of crude oil from soil using air sparging assisted stirred tank reactors. Two surfactants (rhamnolipid and sodium dodecyl sulfate, SDS) were tested and the effects of different parameters (i.e. temperature, surfactant concentrations, washing time, volume/mass ratio) were investigated under varying washing modes namely, stirring only, air sparging only and the combination of stirring and air sparging. The results showed that SDS removed more than 80% crude oil from non-weathered soil samples, whilst rhamnolipid showed similar oil removal at the third and fourth levels of the parameters tested. The oil removal ability of the seawater prepared solutions were better than those of the distilled water solutions at the first and second levels of temperature and concentration of surfactant solutions. This approach of soil washing was noted to be effective in reducing the amount of oil in soil. Therefore we suggested that a field scale test be conducted to assess the efficiency of these surfactants.     

Bioremediation of petroleum hydrocarbon-contaminated soil by composting in biopiles

Composting of contaminated soil in biopiles is an ex situ technology, where organic matter such as bark chips are added to contaminated soil as a bulking agent. Composting of lubricating oil-contaminated soil was performed in field scale ( [Formula: see text] m(3)) using bark chips as the bulking agent, and two commercially available mixed microbial inocula as well as the effect of the level of added nutrients (N,P,K) were tested. Composting of diesel oil-contaminated soil was also performed at one level of nutrient addition and with no inoculum. The mineral oil degradation rate was most rapid during the first months, and it followed a typical first order degradation curve. During 5 months, composting of the mineral oil decreased in all piles with lubrication oil from approximately 2400 to 700 mg (kg dry w)(-1), which was about 70% of the mineral oil content. Correspondingly, the mineral oil content in the pile with diesel oil-contaminated soil decreased with 71% from 700 to 200 mg (kg dry w)(-1). In this type of treatment with addition of a large amount of organic matter, the general microbial activity as measured by soil respiration was enhanced and no particular effect of added inocula was observed.     

微波修复原油污染土壤的均匀设计实验

采用均匀设计实验方法,研究了微波修复原油污染土壤时原油去除率与微波能耗、含水率和含炭率等因素的关系,并应用MATLAB编程拟合出经验公式。结果分析表明:微波能耗在0～288 kJ范围内,污染土壤的原油去除率随微波能耗线性增加;在含水率为6%、含炭率为4%、微波能耗从0增加到288 kJ时,原油去除率从0%增加至92.3%;含炭率在0%～4%范围内原油去除率与含炭率成线性关系,在微波能耗为288 kJ、含水率为6%、含炭率从0%增加到4%时,原油去除率从12.3%增加至92.3%;原油去除率与含水率成二次曲线关系且开口向下,微波修复原油污染土壤的最佳含水率为6.6%。研究结果对微波修复原油污染土壤技术的优化提供了有价值的参考。     

Evaluation of B. subtilis SPB1 biosurfactants' potency for diesel-contaminated soil washing: optimization of oil desorption using Taguchi design

Low solubility of certain hydrophobic soil contaminants limits remediation process. Surface-active compounds can improve the solubility and removal of hydrophobic compounds from contaminated soils and, consequently, their biodegradation. Hence, this paper aims to study desorption efficiency of oil from soil of SPB1 lipopeptide biosurfactant. The effect of different physicochemical parameters on desorption potency was assessed. Taguchi experimental design method was applied in order to enhance the desorption capacity and establish the best washing parameters. Mobilization potency was compared to those of chemical surfactants under the newly defined conditions. Better desorption capacity was obtained using 0.1 % biosurfacatnt solution and the mobilization potency shows great tolerance to acidic and alkaline pH values and salinity. Results show an optimum value of oil removal from diesel-contaminated soil of about 87 %. The optimum washing conditions for surfactant solution volume, biosurfactant concentration, agitation speed, temperature, and time were found to be 12 ml/g of soil, 0.1 % biosurfactant, 200 rpm, 30 °C, and 24 h, respectively. The obtained results were compared to those of SDS and Tween 80 at the optimal conditions described above, and the study reveals an effectiveness of SPB1 biosurfactant comparable to the reported chemical emulsifiers. (1) The obtained findings suggest (a) the competence of Bacillus subtilis biosurfactant in promoting diesel desorption from soil towards chemical surfactants and (b) the applicability of this method in decontaminating crude oil-contaminated soil and, therefore, improving bioavailability of hydrophobic compounds. (2) The obtained findings also suggest the adequacy of Taguchi design in promoting process efficiency. Our findings suggest that preoptimized desorption process using microbial-derived emulsifier can contribute significantly to enhancement of hydrophobic pollutants' bioavailability. This study can be complemented with the investigation of potential role in improving the biodegradation of the diesel adsorbed to the soil.     

工艺参数对表面活性剂洗涤修复PAHs污染土壤的影响

采用土壤洗涤(soil-washing)技术,分别用TritonX-100和Tween-80为强化洗涤剂研究了搅拌强度、洗涤时间、表面活性剂浓度、液固比、温度和间歇搅拌6个工艺参数对PAHs污染土壤洗涤效果的影响。通过一系列烧杯搅拌实验得到最佳洗涤工艺参数。TritonX-100和Tween-80的最佳洗涤时间分别是30 min和60 min,其他工艺参数最佳条件均相同。分别是搅拌强度为250 r/min,表面活性剂浓度为5 g/L,液固比为10∶1,温度为室温和连续搅拌。在此最佳工艺参数条件下,污染土中PAHs的残留率<10%,基本上满足目标污染物的修复目标。应用表面活性剂强化洗涤技术修复PAHs污染土壤是合理和可行的。     

固定化微生物修复石油污染土壤影响因素研究

针对石油污染土壤修复,利用实验室已筛选的高效石油降解单菌SM-3,以天然有机材料为载体,吸附法制备固定化微生物。将游离与固定化微生物应用于室内花盆模拟修复石油污染土壤,对C/N/P、微生物投加量、石油含量、氧化剂和表面活性剂设计5因素4水平正交实验,探讨不同修复时期各影响因素的重要性顺序,最佳条件下各菌株的修复效果。结果表明,不同微生物在不同降解时期,各影响因素的重要性会发生变化;经过21 d的修复,固定化单菌SM-3石油降解率为22.77%,修复过程中,接种量是最重要的影响因素,营养元素N、P投加影响较大,表面活性剂和氧化剂影响次之。     

微米Cu／Fe对污染土壤洗脱液中有机氯农药的降解

以表面活性剂TritonX-100（TX-100）为洗脱剂,某有机氯农药（organochlorinepesticides,OCPs）污染场地土壤为对象,七氯、氯丹和灭蚁灵为目标污染物,研究微米Cu／Fe双金属对污染土壤洗脱液中OCPs的降解效果。考察了洗脱液中OCPs初始浓度、洗脱液pH值、微米零价铁加入量和cu负载量对Cu／Fe去除OCPs效果的影响。结果表明,微米Cu／Fe可以有效的去除土壤洗脱液中目标污染物。当微米零价铁加入量为1．0g（25g／L）,cu负载量为1．0％,洗脱液pH值为6．89时,Cu／Fe对2号土壤洗脱液中七氯、γ-氯丹、α-氯丹和灭蚁灵的去除效果最好,去除率分别为100．0％、99．3％、80．8％和71．1％。洗脱液中OCPs初始浓度越低,微米零价铁加入量越大,Cu／Fe对OCPs去除率越高;偏酸性条件有利于Cu／Fe对γ-氯丹和灭蚁灵的去除,而α-氯丹在中性条件下去除效果最好;1号土壤和2号土壤洗脱液的最佳铜负载量分别为2．O％和1．0％。     

Remediation of cadmium contamination in paddy soils by washing with chemicals: selection of washing chemicals

The efficiencies of neutral salts, strong acids, and chelates were tested for extracting cadmium (Cd) from three paddy soils. The higher the selectivity of the cations of the added neutral salts toward soil adsorption sites, the lower the pH in the extracts and the more soil Cd could be extracted. In addition, soil carbon and nitrogen contents and mineral composition were closely associated with the amount of Cd extracted. Calcium chloride and iron(III) chloride were selected as wash chemicals to restore Cd-contaminated paddy soils in situ. Washing with calcium chloride led to the formation of Cd chloride complexes, enhancing Cd extraction from the soils. The washing also substantially decreased soil levels of exchangeable and acid-soluble Cd, which are the major forms of bioavailable Cd for rice (Oryza sativa L.). The optimum conditions for in situ soil washing were also determined for calcium chloride.     

Decontamination of electronic waste-polluted soil by ultrasound-assisted soil washing

Laboratorial scale experiments were performed to evaluate the efficacy of a washing process using the combination of methyl-β-cyclodextrin (MCD) and tea saponin (TS) for simultaneous desorption of hydrophobic organic contaminants (HOCs) and heavy metals from an electronic waste (e-waste) site. Ultrasonically aided mixing of the field contaminated soil with a combination of MCD and TS solutions simultaneously mobilizes most of polybrominated diphenyl ethers (PBDEs), polychlorinated biphenyls (PCBs), polycyclic aromatic hydrocarbons (PAHs), and the analyte metal (Pb, Cu, and Ni) burdens. It is found that 15 g/L MCD and 10 g/L TS is an efficient reagent combination reconciling extraction performance and reagent costs. Under these conditions, the removal efficiencies of HOCs and heavy metals are 93.5 and 91.2 %, respectively, after 2 cycles of 60-min ultrasound-assisted washing cycles. By contrast, 86.3 % of HOCs and 88.4 % of metals are removed from the soil in the absence of ultrasound after 3 cycles of 120-min washing. The ultrasound-assisted soil washing could generate high removal efficiency and decrease the operating time significantly. Finally, the feasibility of regenerating and reusing the spent washing solution in extracting pollutants from the soil is also demonstrated. By application of this integrated technology, it is possible to recycle the washing solution for a purpose to reduce the consumption of surfactant solutions. Collectively, it has provided an effective and economic treatment of e-waste-polluted soil.