Overestimate of remediation efficiency due to residual sodium persulfate in PAHs contaminated soil and a solution

Oxidation remediation is a commonly used technology for PAHs contaminated soil presently,but the overestimate of efficiency due to ongoing remediation by residual oxidants during extraction and testing has not been paid enough attention.In this study,persulfate was activated by Fe（Ⅱ） to inve stigate the effects of residual oxidants on PAHs removal during detection process and the elimination effects of adding Na₂ SO₃ and extending sampling time on residual oxidants.Results ...     

珠江三角洲地区大气气溶胶中有机污染物背景研究

选择肇庆市鼎湖山自然保护区为珠江三角洲大气气溶胶有机污染评价的区域性环境背景．研究结果表明,珠江三角洲地区大气气溶胶中优控多环芳烃背景值萘、苊、二氢苊、芴、菲、蒽、荧蒽、芘、苯并（a）蒽、、苯并（b）荧蒽、苯并（k）荧蒽、苯并（a）芘、茚并（1,2,3-cd）芘、二苯并（a,h）蒽、苯并（ghi）分别为n.d.、n.d.、tr.、0.14、tr.、0．39、0.53、0.19、1.05、1.82、1.41、0.02、2.29、0.53和2．44ng/m³,总量为10.80ng/m³,其来源主要为高等植物排放.     

多环芳烃在水/有机膨润土间的分配行为

用阳离子表面活性剂（DTMAB、BDTDAB、CTMAB、OTMAB）改性膨润土制得一系列有机膨润土．研究了萘、菲、蒽、苊４种多环芳烃（PAHs）在水／有机膨润土间的分配行为;描述了多环芳烃在水／有机膨润土间的分配系数（K_oc）与有机物本身性质（K_oc、S）之间的关系．结果表明,萘、菲、蒽、苊在水／有机膨润土间的分配系数（K_oc）基本为一常数,与有机膨润土吸附介质无关,相应的分配系数为 2.247×10⁴、2.621×10⁵、2.106×10⁵、5.085×10⁴,其值比多环芳烃在土壤（沉积物）的K_oc大约高10～20倍,这是有机膨润土可用于污染土壤和地下水修复的必要条件之一．     

In situ sequential treatment of a mixed contaminant plume

Groundwater plumes often contain a mixture of contaminants that cannot easily be remediated in situ using a single technology. The purpose of this research was to evaluate an in situ treatment sequence for the control of a mixed organic plume (chlorinated ethenes and petroleum hydrocarbons) within a Funnel-and-Gate. A shallow plume located in the unconfined aquifer at Alameda Point, CA, was found to contain up to 218,000 μg/l of cis-1,2 dichloroethene (cDCE), 16,000 μg/l of vinyl chloride (VC) and <1000 μg/l of 1,1 dichloroethene (1,1 DCE), trans-1,2 dichloroethene (trans-1,2 DCE) and trichloroethene (TCE). Total benzene, toluene, ethylbenzene and xylenes (BTEX) concentrations were <10,000 μg/l. Contaminated groundwater was funneled into a gate, 3.0 m wide, 4.5 m long and 6.0 m deep (keyed into the underlying aquitard) where treatment occurred. The initial gate segment consisted of granular iron, for the reductive dechlorination of the higher chlorinated ethenes. The second segment, the biosparge zone, promoted aerobic biodegradation of petroleum hydrocarbons and any remaining lesser-chlorinated compounds, stimulated by dissolved oxygen (DO) and carbon dioxide (CO₂) additions via an in situ sparge system (CO₂ was used to neutralize the high pH produced from reactions in the iron wall). Groundwater was drawn through the gate by pumping two wells located at the sealed, downgradient, end. Over a 4-month period an estimated 1350 g of cDCE flowed into the treatment gate and the iron wall removed 1230 g, or 91% of the mass. The influent mass of VC was 572 g and the iron wall removed 535 g, corresponding to 94% mass removal. The other chlorinated ethenes had significantly lower influent masses (3 to 108 g) and the iron wall removed the majority of the mass resulting in >96% mass removal for any of the compounds. In spite of these high removal percentages, laboratory column tests indicated that at these levels of chlorinated contaminants, surface saturation of the iron grains likely contributed to lower than expected reaction rates. In the biosparge zone, mass removal of cDCE appeared to occur predominantly by biodegradation (65%) with volatilization (35%) being an important secondary process. The dominant removal process for VC was volatilization (70%) although significant biodegradation was also indicated (30%). Laboratory microcosm results confirmed the potential for aerobic biodegradation of cDCE and VC. When average influent field concentrations for cDCE and VC were 220,000 and 46,000 μg/l, respectively, the sequential treatment unit removed 99.6% of the total mass and when the influent concentrations decreased to 26,000 and 19,000 μg/l for cDCE and VC, respectively, >99.9% removal within the treatment gate was attained. BTEX compounds were found to be significantly retarded in the iron treatment zone. Although they did eventually break through the granular iron, and into the gravel transition zone, none of these compounds was detected in the biosparge zone. No noticeable interferences between the anaerobic (reductive) and aerobic parts of the system occurred during testing. The results of this experiment show that in situ treatment sequences are viable, although further work is needed to optimize performance.     

Effect of electrokinetic transport on the vulnerability of PAH-degrading bacteria in a model aquifer

There has been increasing interest in employing electro-bioremediation, a hybrid technology of bioremediation and electrokinetics, to overcome the low bioavailability of hydrophobic organic contaminants (HOC) by homogenizing sorption-retarded HOC and immobilised microorganisms. Present electro-remediation approaches mainly aim at macroscale pollutant extraction and tend to neglect possible impacts of direct current (DC) on the physiology of microorganisms. The effect of weak electric fields (X = 1 V cm⁻¹) on the fitness of electrokinetically dispersed fluorene-degrading Sphingomonas sp. LB126 in bench-scale model aquifers was investigated by flow cytometry using propidium iodide (PI) as an indicator that distinguishes between PI-permeable (cells with porous membranes, i.e. dead or vulnerable) and PI-impermeable bacteria. After 15.5 h of DC treatment 56% of all cells recovered were dispersed at the centimetre scale relative to 29% in the absence of DC. There was no overall negative effect of the 15.5-h DC treatment on cell vulnerability, as 7.0% of the DC-treated bacteria exhibited PI-staining compared to 6.5% of the control population. Minor differences were observed in the subpopulation that had been mobilised by electroosmosis with an approximately twofold increase in the percentage of PI-stained cells relative to the control. Enhanced PI staining did not correlate with reduced culturability of the cells on rich-medium agar plates. Relative to the control, DC-treated cells mobilised by electroosmosis were threefold more culturable, confirming earlier data that that PI-cell membrane permeability does not always indicate reduced viability of oligotrophic environmental bacteria. Our findings suggest that electrokinetics is a valuable mechanism to transport viable and culturable polycyclic aromatic hydrocarbon (PAH)-degrading bacteria in soil or sediments.     

利用复合酵母菌系统处理含油污泥

利用筛选得到的10株酵母菌组成复合酵母菌系统,并将该复合菌系统接种到泥浆反应器中对模拟油泥样品进行了处理。在对反应器进行优化的基础上,比较了复合酵母菌体系和经驯化的活性污泥体系对模拟风化油泥的处理效果,发现复合酵母菌在反应速度和油去除率上都优于活性污泥。利用GCMS对复合酵母菌处理体系中主要脂肪烃组分的变化进行了分析,结果表明原油组分中脂肪烃部分在处理8d后基本被完全降解。     

人尿中1-羟基芘浓度与多环芳烃日暴露量的关系

采集并分析了 10 0名不吸烟成人 2 4h的呼吸带空气 (PM10 和气相 )、食物及尿液样品 ,建立了尿中1 羟基芘与多环芳烃日暴露量的关系 结果表明 :晨尿 1 羟基芘 (μmol·mol肌酐 -1)浓度与芘、苯并 (a )芘等 13种多环芳烃日暴露量的对数线性回归方程拟合度R2 达 0 12— 0 6 7,方程各项参数也均达到了显著性水平 (P <0 0 0 1)     

氯代芳香族化合物结构-电化学还原电位定量关系的贝叶斯规整化BP神经网络模型

将贝叶斯规整化误差反向传播神经网络(BRBPNN)应用于环境领域的 QSPR模型.采用ChemOffice2004内置的MOPAC 2000计算了6种量子化学参数(分子最高占据能EHOMO、分子最低占据能ELUMO、分子生成热HF、分子偶极矩DIP、分子的电子能量EE和分子的核核排斥能CCR)以及氯原子数(Cl)和分子量(MW),建立了87种氯代芳香族化合物结构与电化学还原电位定量关系的BRBPNN模型.最优网络模型结构为6-20-1,其电化学还原电位的拟合及预测能力明显优于逐步线性回归模型,其训练集和预测集的相关系数平方和均方根误差(MSE)分别达到0.999和0.000105,0.965和 0.00159.最优模型输入节点到隐含层权重平方和的分布规律揭示出各种描述符对还原电位的影响大小依次为: E_LUMO>E_HOMO>HF>CCR>EE>DIP.由散点图揭示出影响为正有EE;影响为负有E_LUMO,HF,DIP;影响无明显正负性的有E_LUMO,CCR.结果表明,贝叶斯规整化大大方便了网络规整化参数选择,保证了网络的优良概括能力和稳健性.本研究对氯代芳香族化合物采用电化学处理的适用性以及分析相应电化学降解机理提供了依据.     

珠江口现代沉积物柱芯样多环芳烃高分辨沉积记录研究

通过对采集于珠江三角洲澳门河口区的沉积物柱状样品中多环芳烃的GC MS定量分析测定,并结合210Pb同位素定年分析,重建了珠江口近代有机污染物的污染史(1959～1996年).研究结果表明,柱芯样品中多环芳烃的浓度为0.6～4.5μg·g-1(干重计),污染程度为中等.其中在20世纪60年代和80年代分别记录到两个高的污染峰,表明这两个时间段内有较大的污染物输入.以母体化合物比值对沉积物样品中的多环芳烃来源进行了分析,结果表明是受到了以油类和不完全燃烧产物为主的混合污染,且污染来源较为单一.对沉积物毒性潜在效应的计算表明,表层沉积物毒性效应较大,且从90年代初期开始后至1996年,毒性当量浓度呈线性趋势增加.     

Effect of housing geometry on the performance of Chemcatcher passive sampler for the monitoring of hydrophobic organic pollutants in water

Passive sampling of pollutants in water has been gaining acceptance for environmental monitoring. Previously, an integrative passive sampler (the Chemcatcher) was developed and calibrated for the measurement of time weighted average concentrations of hydrophobic pollutants in water. Effects of physicochemical properties and environmental variables (water temperature and turbulence) on kinetic and thermodynamic parameters characterising the exchange of analytes between the sampler and water have been published. In this study, the effect of modification in sampler housing geometry on these calibration parameters was studied. The results obtained for polycyclic aromatic hydrocarbons show that reducing the depth of the cavity in the sampler body geometry increased the exchange kinetics by approximately twofold, whilst having no effect on the correlation between the uptake and offload kinetics of analytes. The use of performance reference compounds thus avoids the need for extensive re-calibration when the sampler body geometry is modified.