O3-BAC深度处理工艺中细菌群落时空分布及动态变化规律

为弄清饮用水O₃-BAC深度处理工艺过程中细菌群落的时空分布和动态变化规律,本研究以我国南方某O₃-BAC深度处理工艺水厂为研究对象,采用NovaSeq6000高通量测序技术对夏季和冬季各工艺单元出水及滤砂和活性炭生物膜等细菌群落进行解析.结果表明,出厂水pH、浊度、COD_Mn、菌落总数等指标均满足《生活饮用水卫生标准》（GB5749-2006）的要求.夏季细菌群落多样性明显高于冬季,活性炭生物膜的细菌群落多样性高于滤砂生物膜;混凝沉淀、臭氧化和消毒是影响细菌群落多样性的主要工艺单元.水样和生物膜样品绝对优势菌门均为变形菌门（Proteobacteria）,且主要菌门组成大体相同,但细菌群落门水平相对丰度存在一定的时空差异,属水平上差异则更为明显.此外,检测到的条件致病菌属主要包括芽孢杆菌属（Bacillus）、不动杆菌属（Acinetobacter）、假单胞菌属（Pseudomonas）和分支杆菌属（Mycobacterium）,且其所占核心微生物OTUs数目不受季节性影响.水温和生物可降解溶解性有机碳（BDOC）是显著影响细菌群落分布的主要水质参数.以上研究结果表明,O₃-BAC深度处理工艺过程中细菌群落具有时空变化特性,并可为饮用水微生物安全保障提供支撑.     

模拟土壤淋洗废液中重金属的选择性去除与淋洗液的回收研究

土壤淋洗废液中污染物的选择性去除是实现淋洗液回收的关键.本文以硫化钠（Na₂S）、乙基黄原酸钾（PEX）、二甲基二硫代氨基甲酸钠（DTC）作为重金属沉淀剂处理电子垃圾污染土壤模拟淋洗废液,在筛选出Na₂S作为理想重金属沉淀剂的基础上,研究初始pH值、反应温度、沉淀剂浓度等因素对Na₂S分离络合态重金属的影响,并通过软件模拟和产物表征等方式推测反应机理.结果表明：Na₂S对柠檬酸络合态重金属的分离顺序依次为Cu、Pb、Cd,符合硫化物溶度积原则;反应温度、初始pH值对Na₂S处理络合态重金属无显著影响,重金属去除率均保持在90%以上,柠檬酸的回收率约为95%;Visual MINTEQ模拟结果显示,S^2-投加前液相中重金属主要以H₂CA^-、HCA^2-和CA^3-结合形式存在,S^2-投加后液相中重金属则以HS^-和S^2-结合形式存在;扫描电镜及能谱（SEM-EDS）表明,S^2-与金属阳离子按物质的量比1：1生成硫化物沉淀物,沉淀主要呈团聚、成簇和圆片状存在;X射线衍射（XRD）分析结果表明,沉淀产物中存在CuS、CdS、PbS和CuPbS₂.本研究结果可为化学沉淀法处理重金属污染土壤淋洗废液提供技术参考.     

高原高寒污水处理系统的微生物群落特征

为研究高原高寒污水处理系统活性污泥的微生物群落结构及多样性,以拉萨、云南、四川的3座高原污水厂作为实验组,同时以重庆2座非高原污水厂作为对照,采用PCR-DGGE技术对比分析了高原与非高原污水厂的微生物特性.研究表明：高原污水厂样品与非高原样品在聚类中展现出了较为疏远的关系,微生物群落区别明显.受强紫外线辐照的抑制,高原高寒污水处理系统微生物多样性的平均水平显著低于非高原污水厂,较低的微生物多样性是导致高原高寒地区污染物去除效果不佳的一项重要原因.群落构成方面,共鉴定出16个优势菌属,对应Proteobacteria、Bacteroidetes、Firmicutes、Verrucomicrobia 4个门.组间差异分析结果发现,高原组中丰度显著偏高的菌属只有Prosthecobacter,该菌在污水厂内分布广泛,且能够适应高原低温的条件.对于大多数活性污泥微生物而言,高原强紫外线是不利的生存条件.因此,减少高原露天污水处理系统的紫外辐照,是提升污水处理效能的一个潜在措施.     

Revealing the changes of bacterial community from water source to consumers tap: A full-scale investigation in eastern city of China

This study profiled the bacterial community variations of water from four water treatment systems, including coagulation, sedimentation, sand filtration, ozonation-biological activated carbon filtration (O₃-BAC), disinfection, and the tap water after the distribution process in eastern China. The results showed that different water treatment processes affected the bacterial community structure in different ways. The traditional treatment processes, including coagulation, sedimentation and sand filtration, reduced the total bacterial count, while they had little effect on the bacterial community structure in the treated water (before disinfection). Compared to the traditional treatment process, O₃-BAC reduced the relative abundance of Sphingomonas in the finished water. In addition, ozonation may play a role in reducing the relative abundance of Mycobacterium. NaClO and ClO₂ had different effects on the bacterial community in the finished water. The relative abundance of some bacteria (e.g. Flavobacterium, Phreatobacter and Porphyrobacter) increased in the finished water after ClO₂ disinfection. The relative abundance of Mycobacterium and Legionella, which have been widely reported as waterborne opportunistic pathogens, increased after NaClO disinfection. In addition, some microorganisms proliferated and grew in the distribution system, which could lead to turbidity increases in the tap water. Compared to those in the finished water, the relative abundance of Sphingomonas, Hyphomicrobium, Phreatobacter, Rheinheimera, Pseudomonas and Acinetobacter increased in the tap water disinfected with NaClO, while the relative abundance of Mycobacterium increased in the tap water disinfected with ClO₂. Overall, this study provided the detailed variation in the bacterial community in the drinking water system.     

An investigation of changes in water quality throughout the drinking water production/distribution chain using toxicological and fluorescence analyses

Changes in water quality from source water to finished water and tap water at two conventional drinking water treatment plants(DWTPs) were monitored.Beside the routine water quality testing,Caenorhabditis elegans-based toxicity assays and the fluorescence excitation–emission matrices technique were also applied.Both DWTPs supplied drinking water that met government standards.Under current test conditions,both the investigated finished water and tap water samples exhibited stronger lethal,genotoxic and reprotoxic potential than the relative source water sample,and the tap water sample was more lethal but tended to be less genotoxic than the corresponding finished water sample.Meanwhile,the nearly complete removal of tryptophan-like substances and newly generated tyrosine-like substances were observed after the treatment of drinking water,and humic-like substances were identified in the tap water.Based on these findings,toxic pollutants,including genotoxic/reproductive toxicants,are produced in the drinking water treatment and/or distribution processes.Moreover,further studies are needed to clarify the potentially important roles of tyrosine-like and humic-like substances in mediating drinking water toxicity and to identify the potential sources of these contaminants.Additionally,tryptophan-like fluorescence may be adopted as a useful parameter to monitor the treatment performance of DWTPs.Our observations provided insights into the importance of utilizing biotoxicity assays and fluorescence spectroscopy as tools to complement the routine evaluation of drinking water.     

Removal and desorption of chromium in synthetic effluent by a mixed culture in a bioreactor with a magnetic field

Two chromium removal experiments were performed in bioreactors with and without a magnetic field under the same conditions.The release of the chromium present in the biomass was tested in two experiments one with the initial pH of the medium and one with pH 4.0.The objective was to remove Cr(Ⅵ) and total Cr from the effluent,this was carried out by placing biological treatments of synthetic effluent contaminated with 100 mg/L of Cr(Ⅵ) in a bioreactor with neodymium magnets that applied a magnetic field(intensity85.4 mT) to the mixed culture.The removal of Cr(Ⅵ) was approximately 100.0% for the bioreactor with a magnetic field and 93,3% for the bioreactor without a magnetic field for9 hr of recirculation of the synthetic effluent by the bioreactor.The removal of total Cr was61.6% and 48.4%,with and without a magnetic field,respectively;for 24 hr.The desorption of Cr(VI) in the synthetic effluent was 0.05 mg/L,which is below the limit established by Brazilian legislation(0.1 mg/L) for the discharge of effluent containing Cr(Ⅵ) into bodies of water.The results obtained for the removal of chromium in synthetic effluent suggested that there was no significant influence on the viable cell count of the mixed culture.The desorption of Cr(Ⅵ) in synthetic effluent after bioadsorption of chromium by the mixed culture in the process of removal of chromium in bioreactors with and without a magnetic field was not significant in either of the experiments with different initial pHs.     

精神活性物质在北京市某污水处理厂中的污染特征与生态风险

为了解污水处理厂对精神活性物质的去除特征及总出水对受纳水体的生态风险,采用固相萃取-高效液相色谱-串联质谱法调查了北京市某污水处理厂中13种精神活性物质的浓度水平与负荷量变化,并运用RQ（risk quotient,风险熵）对总出水中精神活性物质进行风险评估.结果表明:①13种精神活性物质在总进水与总出水中均能检出,总质量浓度平均值分别为2 395.10和63.59 ng/L,其中ρ（EPH）（EPH表示麻黄碱）占比分别为93.9%和67.9%,其次为COD（可待因）与METH（甲基苯丙胺）.污水处理厂上游地表水中ρ（EPH）、ρ（METH）与ρ（KET）（KET为氯胺酮）均高于总出水及其下游地表水,说明上游沿河可能有新的污染源输入.②污水处理厂对NK（去甲氯胺酮）、BE（苯甲酰爱康宁）和MTD（美沙酮）均呈负去除,其他精神活性物质的去除主要发生在二级生物处理与三级处理（超滤膜与UV消毒）阶段.③污水处理厂服务区域内精神活性物质的周内负荷量存在一定波动,AMP（苯丙胺）、METH、MDA（3,4-亚甲二氧基苯丙胺）、MDMA（3,4-亚甲二氧基甲基苯丙胺）、KET与HER（海洛因）的负荷量均在周末升高.④污水处理厂总出水中精神活性物质的生态风险均较低（RQ < 0.10）.研究显示,污水处理厂不能完全去除污水中的精神活性物质,总出水中残留精神活性物质对受纳河流生态系统产生的长期混合效应不容忽视.      

平原农区村民居住空间特征与迁居意愿——以江苏省淮安市为例

选择地处苏北平原农区的淮安市所有15510个自然村和872414户农户全样本入户调查数据为分析对象,采用占比统计法和GIS空间分析,对村民居住空间特征与迁居意愿进行研究。主要结论如下：（1）在村落层面,平均规模小,单村独户多且村落分散,多数自然村远离镇区,近一半自然村位居“九靠近一滞洪”区域内。该格局是自然地理条件和人文因素综合影响形成的。（2）在住房层面,农村老旧住房比例高,全市40%农户在城乡同时拥有住房,但在城镇拥有住房率与到城区距离呈负相关,而农村住房空关率则呈现相反的空间格局。（3）在迁居意愿方面,54.1%的农户愿意集中居住且多意向实物安置,较低补偿标准和不便务农是不愿迁居的主要原因;移居城镇是货币安置农户的主要去向,留村和入镇集中居住是实物安置农户的主要去向。在迁居意向农户中,近90%选择政府统建方式,近80%愿意有偿退出宅基地和流转承包地。（4）村民居住空间特征和迁居意愿都存在明显的空间差异,两者之间存有内在联系且均受多种因素影响。     

废旧阴极-赤泥协同处理烧结熟料的溶出性能

采用XRF,ICP-MS,XRD及SEM-EDS检测手段,研究了废旧阴极-赤泥高温协同处理所得熟料的溶出性能.结果表明,Na₂CO₃浓度,温度,时间及液固比因素对Al₂O₃,Na₂O溶出率TFe₂O₃的富集效果的影响趋势一致.最适宜溶出条件为：Na₂CO₃ 30g/L,温度50℃,时间30min,液固比8.该条件下,熟料中Al₂O₃和Na₂O溶出率分别高达为87.41%和92.51%;相应的SiO₂和CaO溶出率仅为3.02%和0.36%,铁矿物几乎不溶.溶出渣中的TFe₂O₃含量从熟料中23.64%提高到39.89%,研究表明溶出工艺同步实现了熟料中铝、钠的回收和铁的富集.再者,处理后溶出渣较熟料减量近16%（以铝和钠溶出率测算）,且属于非危险性废物.