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.     

Fast and efficient aqueous arsenic removal by functionalized MIL-100(Fe)/rGO/δ-MnO2 ternary composites: Adsorption performance and mechanism

Because of its significant toxicological effects on the environment and human health,arsenic(As) is a major global issue.In this study,an Fe-based metal-organic framework(MOF)(Materials of Institut Lavoisier:MIL-100(Fe)) which was impregnated with reduced graphene oxide(rGO) by using a simple hydrothermal method and coated with birnessitetype manganese oxide(δ-MnO_2) using the one-pot reaction process(MIL-100(Fe)/rGO/δ-MnO_2 nanocomposites) was synthesized and applied successfully in As removal.The removal efficiency was rapid,the equilibrium was achieved in 40 min and 120 min for As(Ⅲ) and As(Ⅴ),respectively,at a level of 5 mg/L.The maximum adsorption capacities of As(Ⅲ) and As(Ⅴ) at pH 2 were 192.67 mg/g and 162.07 mg/g,respectively.The adsorbent revealed high stability in pH range 2-9 and saturated adsorbent can be fully regenerated at least five runs.The adsorption process can be described by the pseudo-second-order kinetic model and Langmuir monolayer adsorption.The adsorption mechanisms consisted of electrostatic interaction,oxidation and inner sphere surface complexation.     

Density functional theory (DFT) studies of vanadium-titanium based selective catalytic reduction (SCR) catalysts

Based on density functional theory (DFT) and basic structure models, the chemical reactions on the surface of vanadium-titanium based selective catalytic reduction (SCR) denitrification catalysts were summarized. Reasonable structural models (non-periodic and periodic structural models) are the basis of density functional calculations. A periodic structure model was more appropriate to represent the catalyst surface, and its theoretical calculation results were more comparable with the experimental results than a non-periodic model. It is generally believed that the SCR mechanism where NH₃ and NO react to produce N₂ and H₂O follows an Eley-Rideal type mechanism. NH₂NO was found to be an important intermediate in the SCR reaction, with multiple production routes. Simultaneously, the effects of H₂O, SO₂ and metal on SCR catalysts were also summarized.     

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.      

On-going nitrification in chloraminated drinking water distribution system (DWDS) is conditioned by hydraulics and disinfection strategies

Within the drinking water distribution system (DWDS) using chloramine as disinfectant, nitrification caused by nitrifying bacteria is increasingly becoming a concern as it poses a great challenge for maintaining water quality. To investigate efficient control strategies, operational conditions including hydraulic regimes and disinfectant scenarios were controlled within a flow cell experimental facility. Two test phases were conducted to investigate the effects on the extent of nitrification of three flow rates (Q = 2, 6, and 10 L/min) and four disinfection scenarios (total Cl₂=1 mg/L, Cl₂/NH₃-N=3:1; total Cl₂=1 mg/L, Cl₂/NH₃-N=5:1; total Cl₂=5 mg/L, Cl₂/NH₃-N=3:1; and total Cl₂=5 mg/L, Cl₂/NH₃-N=5:1). Physico-chemical parameters and nitrification indicators were monitored during the tests. The characteristics of biofilm extracellular polymetric substance (EPS) were evaluated after the experiment. The main results from the study indicate that nitrification is affected by hydraulic conditions and the process tends to be severe when the fluid flow transforms from laminar to turbulent (2300<Re<4000). Increasing disinfectant concentration and optimizing Cl₂/NH₃-N mass ratio were found to inhibit nitrification to some extend when the system was running at turbulent condition (Q = 10 L/min, Re = 5535). EPS extracted from biofilm that was established at the flow rate of 6 L/min had greater carbohydrate/protein ratio. Furthermore, several nitrification indicators were evaluated for their prediction efficiency and the results suggest that the change of nitrite, together with total organic carbon (TOC) and turbidity can indicate nitrification potential efficiently.     

国内外饮用水余氯限值及监测方法的研究进展

新型冠状病毒肺炎疫情期间大规模使用含氯消毒剂,其残留可能对水环境及人体健康造成影响.我国饮用水水源地质量标准并未设置余氯项目及其浓度限值,且缺乏统一的余氯现场快速分析方法标准.为公共卫生事件发生期间的水质余氯监测与评价提供参考,对国内外饮用水标准余氯限值、实验室标准分析方法、现场快速分析方法等进行汇总分析,结果表明:①不同国家和地区以及WHO（World Health Organization,世界卫生组织）在饮用水标准中分别设置了出厂水中余氯限值（范围为0.1~2.0 mg/L）、管网末梢水中余氯限值（范围为0.1~1.8 mg/L）及饮用水中余氯最大允许浓度（范围为4~5 mg/L）.②比色法、容量法因其具有反应迅速且稳定、准确度及精密度较高等优点而成为国内外实验室主要标准或推荐分析方法,高效液相色谱法检出限最低,灵敏度最高,可用于余氯痕量分析.③余氯现场快速分析方法多以比色法为主,在线监测方法多为电化学方法,但缺乏统一的标准方法.研究显示,国外饮用水标准中余氯最大允许浓度为5 mg/L,WHO推荐高风险环境下的管网末梢余氯浓度最低为0.5 mg/L,建议尽快开展水质余氯现场监测方法标准化研究.      

闽江河口养虾塘养殖期和非养殖期CO2通量变化特征

为揭示河口区陆基养虾塘从养殖期到非养殖期一年间的CO₂通量变化,以福建省闽江河口鳝鱼滩陆基养虾塘为研究对象,于2016年5月-2017年3月采用悬浮箱/静态箱-气相色谱法对养虾塘养殖期水-大气界面和非养殖期沉积物-大气界面白天CO₂垂直通量进行原位观测.结果表明:①养虾塘在整个研究期间CO₂通量变化范围为-62.87~162.81 mg/（m2·h）,平均值为（42.66±18.12）mg/（m2·h）,总体上表现为大气CO₂的释放源,且呈非养殖期CO₂通量平均值[（78.51±16.61）mg/（m2·h）]显著高于养殖期[（17.98±18.26）mg/（m2·h）]的特征.②养殖期间,养虾塘CO₂通量呈"排放-吸收"交替变化的特征,而非养殖期养虾塘一直是大气CO₂的净排放源.③养虾塘养殖期CO₂通量时间变化特征主要受到ρ（DOC）（DOC为总溶解有机碳）、ρ（SO₄2-）、ρ（Cl-）、盐度、pH、ρ（Chla）（Chla为叶绿素a）的影响,其中,pH和ρ（SO₄2-）是其主要影响因子,而ρ（TDN）（TDN为总溶解氮）、ρ（TDP）（TDP为总溶解磷）、ρ（SO₄2-）对非养殖期CO₂通量时间变化影响较大.研究显示,滨海陆基养殖塘是大气CO₂的重要来源,其排放通量多低于河流、水库等水生生态系统,但高于湖泊生态系统;养殖塘CO₂通量受人为影响明显,其较高的变异性与养殖生物、饲料投放以及浮游藻类有关.      

废塑料再生过程废水中微塑料去除模拟试验

微塑料是一种存在于不同环境介质中的新兴污染物,主要来源于废弃塑料制品,其存在污染范围广、潜在环境污染大的问题.废塑料再生企业生产废水中微塑料浓度远高于其他类型废水,对其生产废水中的微塑料进行处理具有重要的环境意义.模拟废塑料再生过程的生产废水并进行微塑料去除的絮凝沉淀试验,研究絮凝剂投加量、pH、水力快速搅拌条件的单因素和正交试验对废水中微塑料去除率及其各因素作用的影响.结果表明:①当PAC (聚合氯化铝)投加量为10 mL,PAM (聚丙烯酰胺)投加量为7 mL,pH为9,水力快速搅拌条件为100 r/min下维持40 s再200 r/min下维持40 s时,微塑料的总去除率最高,达91%.②PAC投加量是影响微塑料去除效果的主要因素,其次是pH.③微塑料的去除率与其本身的密度有关,密度大的ABS (acrylonitrile butadiene styrene,丙烯腈-丁二烯-苯乙烯)去除率最高,密度小的PE (polyethylene,聚乙烯)去除率最低.④不同粒径区间的微塑料去除率区别较大,粒径小(0.1~0.25 mm)的微塑料去除效果最好.研究显示,通过控制PAC和PAM的投加量、pH和水力搅拌速率等条件,能够有效将废水中的微塑料通过絮凝沉淀的方法去除,从而达到净化含微塑料生产废水的目的.      

特殊区域地表水环境背景值表征技术方法研究与应用

选取黑龙江省源头水保护区作为研究对象,根据DEM数据对保护区内随机布设的水质监测点控制单元进行划分并提取单元内的相关指标建立监测点背景特性量化模型,基于量化结果提出地表水环境背景值监测方案,建立背景值数据库.选取研究区自然属性指标与空间属性指标,以空间叠置技术与聚类分析方法对研究区地表水进行背景值分区,最终将黑龙江省分为六大地表水水质背景值地理分区,并计算了各分区地表水环境背景值表征范围.表征范围显示：依据现行标准进行水质评价,保护区内水质背景值已超出Ⅱ类水质标准限值.因此,基于水质背景值研究成果提出了考虑背景值影响下的水环境质量评价方法,并将方法应用于研究区,结果表明方法切实可行且优于单因子评价法.研究成果可为区域制定背景值影响下的水环境评价方法提供科学的数据支撑与理论依据.