粤港澳大湾区NO2污染的时空特征及影响因素分析

利用Aura卫星搭载的臭氧观测仪（OMI）反演的对流层NO₂柱密度数据,分析了自2005年以来粤港澳大湾区（GBA）对流层NO₂柱密度的空间分布特征、时间变化趋势及其影响因素.研究结果表明GBA对流层NO₂柱密度从2005~2018年呈减少的趋势,每年递减约为2.8%.小波系数显示时间演化过程中存在9个月的主振荡周期,冬季浓度较高,夏季较低.人为排放和各种自然因素,导致了GBA对流层NO₂柱浓度月变化在时间和空间上存在明显差异,最小值和最大值分别出现在6和12月,多年平均值分别为3.9665×10¹⁵和12.3423×10¹⁵molec/cm².NO₂在空间分布上呈现明显的空间分异特征,冬季12月最明显.NO₂污染严重的高值区主要出现在中部地区,如广州市、佛山市和中山市,最大的对流层NO₂柱密度可达18.8306×10¹⁵molec/cm²,大约是周边地区的3 倍,且高污染区域向四周逐渐扩散,连成一片.低值区主要在北部的肇庆市和东部的惠州市,多年平均的对流层NO₂柱密度约为7.1400×10¹⁵molec/cm².对流层NO₂柱密度的增长率在不同区域的变化趋势呈现明显的差异,变化范围为-15×10¹⁵~6×10¹⁵molec/cm²,增长率百分比范围为-65%~65%.出现增长的地区主要是肇庆市北部和惠州市东部的低值区;对流层NO₂出现明显减少的区域集中在中部的高值区,减少量最大的地区为广州市、佛山市和中山市交界处.     

浙江典型海湾潮间带沉积物污染及生态风险评价

基于浙江4个典型海湾潮间带表层沉积物重金属元素Cu、Zn、Pb、Cr、Cd、Hg、As和多氯联苯（PCB）的调查结果,探究其污染特征、潜在生态风险和来源.结果表明,海湾潮间带表层沉积物Cd、Hg、As、PCB含量均符合国家海洋沉积物质量Ⅰ类标准;42%、9%、3%、12%站位的Cu、Zn、Pb、Cr符合国家海洋沉积物质量II类标准,1%站位的Cu和Zn符合国家海洋沉积物质量III类标准.区域污染程度（PLI_zone）依次为乐清湾 > 三门湾 > 象山港 > 杭州湾,乐清湾潮间带沉积环境为中等污染,杭州湾、象山港和三门湾潮间带沉积环境无污染.区域生态风险（RI）依次为乐清湾 > 杭州湾 > 三门湾 > 象山港,乐清湾和杭州湾潮间带沉积物为中潜在生态风险,三门湾和象山港潮间带沉积物为低潜在生态风险.Cd是首要的潜在生态风险因子,Cd对杭州湾、象山港、三门湾、乐清湾潜在生态风险指数（RI）的贡献分别为63%、54%、58%和55%.生活污水、工农业和交通污染是浙江典型海湾潮间带重金属和PCB的主要来源.     

滆湖水华初期浮游植物群落特征及与水环境因子相关性分析

为探究滆湖水华初期浮游植物群落特征及与水环境因子的相关性,于2018年5—7月在全湖布设22个点,调查研究滆湖水华初期浮游植物群落时空分布特征,并对引起水华主导环境因子进行分析.结果表明：①共获得7门119属,优势属为绿藻门的小球藻与球团藻、蓝藻门的鞘丝藻与微囊藻,其中湖心区域浮游植物丰度与多样性小,均匀性低,属于中偏重污染区域;湖北区以北属于中污染区域,蓝藻堆积严重;西部沿岸及南端区域属于中偏轻污染区域.②冗余分析得出,湖心藻类与水温（T）有强相关性,与叶绿素a（Chl-a）、溶解性总磷（DTP）、pH、溶解氧（DO）呈一定正相关性;湖北区以北藻类与底泥有机质（OM）、水体悬浮物（SS）、Chl-a及DTP呈强相关性,与T呈一定相关性.T与多项环境因子相关,均值从26.1℃上升到32.4℃;OM与有机磷（OP）呈高度相关性（p<0.05,r=0.892）.水华发生的主导环境因子为T、DTP与pH,底泥OM及OP有一定影响.     

南京市饮用水源地抗生素污染特征及风险评估

采用固相萃取-液相色谱-串联质谱技术（SPE-HPLC-MS/MS）,对南京市饮用水源地抗生素含量及分布特征进行了分析.结果表明,17个采样点总浓度为0.56~1994.96 ng·L^-1,共检出5种大环内酯类、13种磺胺类、3种四环素类、8种喹诺酮类抗生素,平均浓度为0.30~37.07 ng·L^-1,其中检出浓度最高的抗生素为环丙沙星（CIP）,浓度为317.60 ng·L^-1,检出率最高的抗生素为克林霉素（CLI）,检出率为88.24%.与国内部分河流相比,南京市饮用水源地水体中大环内酯类、四环素类、喹诺酮类抗生素残留浓度处于较高水平.生态风险评估结果表明,点位S7具有最高的联合风险熵值（24.58）,氧氟沙星（OFX）的风险熵值最高,达到13.06;健康风险评估结果表明,9种抗生素对人体健康的风险熵Q_H为1.70×10^-3~9.47,强力霉素（DOX）、诺氟沙星（NOR）、恩诺沙星（ERX）、CIP和OFX对大部分年龄段的人体健康具有高水平风险.     

滇黔桂岩溶区河漫滩土壤重金属含量、来源及潜在生态风险

利用全国地球化学基准计划在滇黔桂岩溶区35个点位采集的70件河漫滩表、深层土壤样品,分析了As、Cd、Cr、Cu、Hg、Ni、Pb和Zn 8种重金属元素含量特征,探究了重金属来源、污染状况及潜在生态风险.结果表明,8种重金属元素含量大部分均高于全国土壤背景值,在滇东南地区含量最高,桂西北地区最低.表层土壤Cd、Hg明显富集,As、Cr、Cu、Ni与深层土壤含量相当;As、Cd、Hg、Pb、Zn在农田、菜地中明显高于深层土壤,Cr、Cu和Ni在各类土地中与深层土壤相当.因子分析结果显示,表层土壤中Cd、Cr、Cu、Ni受地质背景控制,As、Pb、Zn既与地质背景有关,也受人为活动影响,Hg受人为活动影响较严重;深层土壤中Cd、Cr、Cu、Ni、Cr、Zn继承了区域母岩特征,As、Hg和Pb受地质背景和人为活动双重影响.地累积指数法和富集因子法污染评价结果表明,研究区河漫滩表层土壤中Cd、Hg污染较重,As、Cr、Cu、Ni、Pb、Zn大部分为轻度污染或无污染.各重金属潜在生态风险指数高低顺序依次为Hg > Cd > As > Cu > Ni > Pb > Cr > Zn,Cd和Hg的生态风险指数之和占综合指数的82.43%,生态风险最高;滇东南地区重金属潜在风险综合指数最高,具重度生态风险.     

北方湖库沉积物重金属区域特征及生态风险评价

以白洋淀、衡水湖、于桥水库、松花湖、大伙房水库和小兴凯湖沉积作为研究对象,通过对北方六湖库沉积物中Cu、Zn、Pb、Cr、Ni等重金属元素进行分析,并与国内外其他水域重金属污染情况进行多因素比较,探讨了六湖库主要重金属污染源的差异性,区域分布特征以及与国内外其他水域污染的相似性和区别.结果表明,六湖库沉积物重金属污染处于中等偏下水平.六湖库之间主要重金属污染源存在差别.沉积物重金属含量未出现明显上升的趋势.其中Zn、Pb存在富集现象,但Pb含量与历史数据相比出现下降,Zn的含量与其他地区相比整体偏高.大伙房水库沉积物重金属污染较重,Cu、Zn、Pb、Cr、Ni含量平均值分别为56.28,142.3,17.44,97.9,44.44mg/kg.小兴凯湖沉积物重金属含量最低,Cu、Zn、Pb、Cr、Ni含量平均值分别为2.41,63.90,13.37,56.36,26.09mg/kg.六湖库综合风险评价结果为大伙房水库>于桥水库>白洋淀>衡水湖>松花湖>小兴凯湖,重金属整体潜在生态风险指数为低.     

2018年春节期间京津冀地区污染过程分析

为了解2018年春节期间京津冀地区空气污染情况,利用近地面污染物浓度数据、激光雷达组网观测数据,结合WRF气象要素、颗粒物输送通量和HYSPLIT气团轨迹综合分析污染过程.结果表明,春节期间出现3次污染过程.春节前一次污染过程,各站点PM_2.5浓度均未超过200μg/m³;除夕夜,廊坊站点PM_2.5峰值浓度达到504μg/m³,是清洁天气的26倍;年初二~初五,各站点PM_2.5始终高于120μg/m³,且污染主要聚集在500m高度以下,北京地区存在高空传输,800m处最大输送通量达939μg/（m³·s）,此次重污染过程为一次典型的区域累积和传输过程.京津冀地区处于严格管控状态时,燃放烟花爆竹期间PM_2.5峰值浓度可达无燃放时PM_2.5峰值的3.2倍.为防止春节期间重污染现象的发生,需对静稳天气下燃放烟花炮竹采取预防对策.     

Influence of floc dynamic protection layer on alleviating ultrafiltration membrane fouling induced by humic substances

Cake layer formation is inevitable over time for ultrafiltration (UF) membrane-based drinking water treatment. Although the cake layer is always considered to cause membrane fouling, it can also act as a “dynamic protection layer”, as it further adsorbs pollutants and dramatically reduces their chance of getting to the membrane surface. Here, the UF membrane fouling performance was investigated with pre-deposited loose flocs in the presence of humic acid (HA). The results showed that the floc dynamic protection layer played an important role in removing HA. The higher the solution pH, the more negative the floc charge, resulting in lower HA removal efficiency due to the electrostatic repulsion and large pore size of the floc layer. With decreasing solution pH, a positively charged floc dynamic protection layer was formed, and more HA molecules were adsorbed. The potential reasons were ascribed to the smaller floc size, greater positive charge, and higher roughness of the floc layer. However, similar membrane fouling performance was also observed for the negative and positive floc dynamic protection layers due to their strong looseness characteristics. In addition, the molecular weight (MW) distribution of HA also played an important role in UF membrane fouling behavior. For the small MW HA molecules, the chance of forming a loose cake layer was high with a negatively charged floc dynamic protection layer, while for the large MW HA molecules it was high with a positively charged floc dynamic protection layer. As a result, slight UF membrane fouling was induced.     

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.     

Recent advances in catalytic decomposition of ozone

Ozone (O₃), as a harmful air pollutant, has been of wide concern. Safe, efficient, and economical O₃ removal methods urgently need to be developed. Catalytic decomposition is the most promising method for O₃ removal, especially at room temperature or even subzero temperatures. Great efforts have been made to develop high-efficiency catalysts for O₃ decomposition that can operate at low temperatures, high space velocity and high humidity. First, this review describes the general reaction mechanism of O₃ decomposition on noble metal and transition metal oxide catalysts. Then, progress on the O₃ decomposition performance of various catalysts in the past 30 years is summarized in detail. The main focus is the O₃ decomposition performance of manganese oxides, which are divided into supported manganese oxides and non-supported manganese oxides. Methods to improve the activity, stability, and humidity resistance of manganese oxide catalysts for O₃ decomposition are also summarized. The deactivation mechanisms of manganese oxides under dry and humid conditions are discussed. The O₃ decomposition performance of monolithic catalysts is also summarized from the perspective of industrial applications. Finally, the future development directions and prospects of O₃ catalytic decomposition technology are put forward.