PFOS前体物质(PreFOSs)降解菌的分离鉴定及其降解特性

从氟化工厂附近土壤中分离出1株能以全氟辛烷磺酸前体物质(Pre FOSs)为唯一碳源和能源生长的降解菌PF1,经形态观察及16S r DNA基因序列分析,初步鉴定该菌为生丝微菌属(Hyphomicrobium sp.).在温度为30℃、p H为7.0~7.2条件下,菌株PF1对全氟辛基磺酰胺(PFOSA)和N-乙基全氟辛基磺酰胺(N-Et FOSA)48 h降解率分别为14.6%和8.2%,对PFOS无降解能力.对降解产物进行检测和分析,结果表明PFOSA的降解产物为PFOS;N-Et FOSA能被降解生成PFOSA和PFOS,同时也产生少量的全氟辛基磺酰胺乙酸(FOSAA).由此推断Pre FOSs降解途径,在菌株PF1的作用下,PFOSA脱去氨基直接转化成PFOS.NEt FOSA主要有2种降解途径:(1)N-Et FOSA脱乙基产生PFOSA,PFOSA再进一步脱氨基生成PFOS,此为主要途径;(2)NEt FOSA中的N-乙基被氧化成乙酸基生成FOSAA,FOSAA进一步脱去乙酸基生成PFOSA,并最终脱氨基生成PFOS.     

巯基改性高岭土负载CeO2-CdS光催化降解结晶紫

为获得高效催化活性的光催化材料,实现偶氮类染料的高效降解,试验以巯基乙酸钠作为硫源和高岭土改性剂合成了巯基高岭土/CeO₂-CdS催化剂,并以降解结晶紫为模板反应,优化确定了巯基高岭土/CeO₂-CdS催化剂的制备条件.采用XRD（X射线衍射）、SEM（扫描电子显微镜）、TEM（透射电子显微镜）、FTIR（傅里叶红外光谱）和UV-Vis（紫外-可见光漫反射光谱）对催化剂进行了表征.结果表明:①催化剂是由巯基高岭土、立方相结构的CdS和萤石结构的CeO₂组成;②CdS和CeO₂的负载破坏了巯基高岭土的层状结构;③最优催化剂和巯基高岭土/CeO₂的可见光的响应范围分别为550和450 nm;④当CeO₂:CdS（摩尔比,下同）为4:6,巯基高岭土:CeO₂-CdS（质量比,下同）为1:3时,催化剂具有最优的光催化活性;⑤在50 mL结晶紫浓度为10 mg/L的溶液中,添加0.1 g最优催化剂后,采用350 W氙灯对其光照150 min时,结晶紫的降解率为95.1%;⑥最优催化剂具有良好的重复使用性能,重复使用5次时,对结晶紫的降解率为90.4%.研究显示,结晶紫降解的最终产物为CO₂和H₂O,催化剂对结晶紫的降解机理是以羟基自由基氧化为主和超氧基氧化为辅的共存氧化机理.      

海藻酸钠包埋活性炭与细菌的条件优化及其对Pb~(2+)的吸附特征研究

利用海藻酸钠固定化包埋活性炭与多黏类芽孢杆菌GA1,通过正交试验研究海藻酸钠溶液浓度、包炭量及包菌量吸附Pb2+的最佳配比,并研究了这种新型的固定化小球对Pb2+的吸附特征.结果表明,固定化活性炭与多黏类芽孢杆菌GA1小球最佳制备条件为海藻酸钠质量分数2.5%、包炭量1:20和包菌量1:2,在该制备条件下吸附率达到93.74%.固定化小球的最佳吸附条件为pH5、温度30℃和Pb2+初始浓度300mg·L-1,活性炭与GA1经固定后对pH、温度和Pb2+初始浓度适应范围扩大.吸附平衡曲线表明,对Pb2+的吸附在30min内是一个快速的过程,在2h时基本趋于平衡,且平衡曲线能较好地用Langmuir模型和Freundlich模型来描述,其吸附过程主要为单分子层吸附,最大单分子层吸附量为370.37mg·g-1.解吸结果表明固定化小球能有效地循环利用.     

改性粉煤灰在处理锑矿选矿废水中的应用

针对锑矿选矿废水中锑和丁基黄原酸钠严重超标的问题,用酸改性粉煤灰对其进行吸附处理.试验结果表明,当改性粉煤灰处理选矿废水的最佳质量体积比(g.mL-1)为1:100,pH值为3,静置时间为4h时,可以将选矿废水中的锑浓度从28.611mg.L-1降到0.05mg.L-1以下,去除率达99.8%以上;废水中的丁基黄原酸钠浓度可从0.373mg.L-1降到0.02mg.L-1以下,去除率达95.0%以上.处理废水后的改性粉煤灰用硫酸-硝酸浸提,浸出液中重金属离子浓度均低于国家浸出毒性标准,表明改性粉煤灰是一种很好的锑矿选矿废水处理剂.     

Determination of polyfluoroalkyl compounds in water and suspended particulate matter in the river Elbe and North Sea, Germany

The distribution of polyfluoroalkyl compounds (PFCs) in the dissolved and particulate phase and their discharge from the river Elbe into the North Sea were studied. The PFCs quantified included C₄-C₈ perfluorinated sulfonates (PFSAs), 6:2 fluorotelomer sulfonate (6:2 FTS), C₆ and C₈ perfluorinated sulfinates (PFSiAs), C₄-C₁₂ perfluorinated carboxylic acids (PFCAs), perfluoro-3,7-dimethyl-octanoic acid (3,7m₂-PFOA), perfluorooctane sulfonamide (FOSA), and n-ethyl perfluroctane sulfonamidoethanol (EtFOSE). PFCs were mostly distributed in the dissolved phase, where perfluorooctanoic acid (PFOA) dominated with 2.9–12.5 ng/L. In the suspended particulate matter FOSA and perfluorooctane sulfonate (PFOS) showed the highest concentrations (4.0 ng/L and 2.3 ng/L, respectively). The total flux of ΣPFCs from the river Elbe was estimated to be 802 kg/year for the dissolved phase and 152 kg/year for the particulate phase. This indicates that the river Elbe acts as a source of PFCs into the North Sea. However, the concentrations of perfluorobutane sulfonate (PFBS) and perfluorobutanoic acid (PFBA) in the North Sea were higher than that in the river Elbe, thus an alternative source must exist for these compounds.     

Selective sorption of perfluorooctane sulfonate on molecularly imprinted polymer adsorbents

Perfluorooctane sulfonate (PFOS), as a potential persistent organic pollutant, has been widely detected in water environments, and has become a great concern in recent years. PFOS is very stable and difficult to decompose using conventional techniques. Sorption may be an attractive method to remove it from water. In this study, the molecularly imprinted polymer (MIP) adsorbents were prepared through the polymerization of 4-vinylpyridine under different preparation conditions in order to remove perfluorooctane sulfonate (PFOS) from water. The MIP adsorbents using perfluorooctanoic acid (PFOA) as the template had good imprinting effects and could selectively remove PFOS from aqueous solution. The sorption behaviors including sorption kinetics, isotherms, and effect of pH, salt, and competitive anions were investigated. Experimental results showed that the sorption of PFOS on the MIP adsorbents was very fast, pH-dependent, and highly selective. The achieved fast sorption equilibrium within 1 h was attributed to the surface sorption on the fine adsorbents. The sorption isotherms showed that the sorption selectivity of PFOS on the MIP adsorbents decreased at high PFOS concentrations, which may be due to the double-layer sorption and the formation of PFOS micelles on the sorbent surface. The sorption of PFOS on the MIP adsorbents was mainly dominated by the electrostatic interaction between the protonated vinylpyridine on the adsorbent surface and the anionic PFOS. The prepared MIP adsorbents can potentially be applied in water and wastewater treatment for selective removal of PFOS.     

珠江口水环境中多溴联苯醚生态风险分析

以多溴联苯醚(PBDEs)作为研究对象,对珠江口水环境中多溴联苯醚进行了生态风险问题形成、生态风险分析及生态风险表征。研究结果表明,珠江口水环境中多溴联苯醚的生态风险主要来自五溴联苯醚,其在水相和沉积物相中的计算结果分别为0.000057和0.0073,目前珠江口水环境中多溴联苯醚的生态风险水平较低,暂无生态风险。     

去除煤矿生活污水二级生化处理出水中NH3-N的试验研究

采用间歇式静态杯罐试验方法,对残余NH3-N浓度5～15mg/L的某煤矿生活污水二级生化处理出水进行了次氯酸钠氧化法去除研究,考察了不同的次氯酸钠溶液投加量和不同反应时间等因素对NH3-N去除效果的影响,研究了反应期间pH的变化情况。试验结果表明,次氯酸钠氧化法可以有效地去除残余NH3-N,对于本试验中的某煤矿生活污水二级生化处理出水,在最佳次氯酸钠投药量为0.1%（Vcl/VH2O）,最佳反应时间在30～50min,其对NH3-N去除率为65.3%,经过氧化处理后,其水质可以达到工业循环冷却水处理设计规范（GB50050-2007）中对NH3-N≤5mg/L的要求。     

纳米铁系材料与反硝化细菌复合去除地下水硝酸盐氮研究

采用不同液相还原法制备了纳米Fe、纳米Fe/Ni和油酸钠包覆型纳米Fe粒子,并将其与反硝化细菌复合应用于地下水中硝酸盐氮的去除研究中.分别考察了不同纳米铁系材料与反硝化细菌复合体系去除硝酸盐氮的反应速率及对脱氮产物生成的影响.同时,从核糖核酸(RNA)水平考察了不同纳米铁系材料对反硝化细菌的影响.结果表明,纳米Fe/Ni复合体系脱氮速率最快,6d内对硝酸盐氮的去除率可达到100%,最终产物主要为氨氮,占体系总氮的69%;而纳米Fe和油酸钠包覆型纳米Fe复合体系9d可将硝酸盐氮100%去除,氨氮的转化率分别为52%和16%.另外,从反应前后反硝化细菌总RNA浓度的变化情况看,纳米Fe/Ni复合体系、纳米Fe复合体系和油酸钠包覆型纳米Fe复合体系的反硝化细菌总RNA浓度分别降低了93%、40%和34%,可见3种纳米铁系材料对反硝化细菌毒性大小顺序为:纳米Fe/Ni纳米Fe油酸钠包覆型纳米Fe.     

Effect of chemical and thermal activations on the properties of rice husk ash-based solidified wastes

Strength development,leachability and microstructure of heavy metals from the solidified waste using synthesis rice husk ash (sRHA) and lime blended at the weight ratio of 1:1 were used as binders.The heavy metal-containing sludge was used at the level of 0 wt.%,30 wt.%,and 50 wt.% dry weight,respectively.The sample specimens with and without 1.5 wt.% of sodium silicate (SiO 2 /Na 2 O=1.0) were cured under the ambient condition and elevated temperature curing at 50°C for 24 hr.Experimental results showed that the introduction of sodium silicate solution and elevated temperature curing to sRHA-based solidified waste containing 30 wt.% of heavy metal sludge gave one day strength of 20 kg/cm 2 compared to 0.9 kg/cm2 for the control sample.XRD patterns indicated that most metal-sulfides present in the sludge were appeared in the solidified waste and SEM coupled with EDX techniques reveal these metal-sulfide particles were trapped within the lime-sRHA matrices.In addition,cumulative leaching behavior by tank test (EA NEN 7375:2004) showed that solidified waste containing up to 30 wt.% of heavy metal sludge was suitable to dispose in a secured landfill.