固定化微藻流化床反应器去除低碳污水中氨氮的潜力

以固定化微藻颗粒为原料,通过搭建流化床反应器强化微藻对氨氮（NH₄⁺-N）的去除,设计了藻种、污水上升流速、光周期和光照强度四组单一变量实验,系统地研究了不同条件下微藻去除NH₄⁺-N的能力.结果表明,当以固定化斜生栅藻为原料、污水上升流速为6.8m/h、光周期为8：16h和光照强度为4800Lux时,NH₄⁺-N去除效果最优（96.7%）.在最优操作条件下,探究了COD为200mg/L时微藻去除NH₄⁺-N的潜力,结果表明,当NH₄⁺-N初始浓度不高于50mg/L时,NH₄⁺-N去除率高于95%.本实验建立了一套半连续微藻流化床实验方法,该方法显著减弱了微藻在生物同化过程中对有机碳源的依赖性,为低COD条件下微藻生物脱氮工艺的设计提供了技术参考和理论基础.     

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.     

黄土高原人工刺槐林土壤团聚体中不同活性有机碳从南到北的变化特征

不同粒径团聚体中的不同活性有机碳对人工林土壤质量改善及碳库动态平衡有重要的作用.本研究在黄土高原地区,从南向北沿着降雨和温度降低梯度选择淳化、安塞、绥德和神木共4个地区,比较研究了人工刺槐林土壤团聚体不同的活性有机碳含量变化及其影响因素.通过湿筛法将土壤团聚体分级为粉黏粒（<0.053 mm）、微团聚体（0.25~0.053 mm）和大团聚体（>0.25 mm）,用Leffory法测定3种粒径土壤团聚体低、中、高活性有机碳含量.结果表明：①4个样区大团聚体（>0.25 mm）含量由南至北呈先降低后增加趋势,微团聚体（0.25~0.053 mm）含量逐渐增加,粉黏粒（<0.053 mm）含量则先增后减.②4个样区中土壤团聚体3种活性有机碳含量大小顺序为低活性 > 中活性 > 高活性,其中,粉黏粒（<0.053 mm）低活性有机碳含量为1.02~1.52 g·kg^-1,中活性有机碳含量为0.53~0.91 g·kg^-1,高活性有机碳含量为0.28~0.43 g·kg^-1;而微团聚体（0.25~0.053 mm）低活性有机碳含量为1.02~2.02 g·kg^-1,中活性有机碳含量为0.46~1.20 g·kg^-1,高活性有机碳含量为0.31~0.85 g·kg^-1;大团聚体（>0.25 mm）低活性有机碳含量为1.08~3.07 g·kg^-1,中活性有机碳含量为0.70~1.96 g·kg^-1,高活性有机碳含量为0.48~1.24 g·kg^-1.③黄土高原人工刺槐林3种粒径团聚体的低、中、高活性有机碳含量主要与年均气温（MAT）、年均降雨量（MAP）、土壤SOC、TN和含水率显著相关（p<0.05）,且在同一活性下,活性有机碳含量与MAT、MAP、土壤TN、SOC、含水率的相关性随着土壤团聚体粒径的增大而越显著.研究结果对理解黄土高原土壤团聚体活性有机碳含量在空间尺度上的变化特征和影响因素具有重要意义.     

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.     

Ca(OH)2解吸并固定混合吸收液中CO2的实验研究

CO₂化学吸收法分离纯度高,技术成熟,但能耗过高及成本是困扰该技术发展的瓶颈.在常压条件下对利用Ca（OH）₂直接矿物碳酸化固定MDEA/PZ混合吸收富液中CO₂进行了一系列实验研究,考察了吸收液负荷、Ca（OH）₂投加量、pH、温度及搅拌速率等因素对解吸率的影响,并利用动态吸收-解吸循环实验研究了其CO₂吸收性能和循环使用稳定性,最后对碳酸化反应产物进行了XRD、TEM分析.结果表明,在常压条件下,Ca（OH）₂可以通过液相直接矿物碳酸化对CO₂进行直接固定,并实现吸收富液的再生;随着负荷的升高及Ca（OH）₂投加量、pH、搅拌速率的增大,解吸率随之增加;随着溶液温度升高,解吸率下降;经过5次动态吸收-解吸循环实验后CO₂吸收量可以达到并保持在0.57 mol·L^-1,显示出了良好的循环稳定性.     

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.     

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.     

Tuning the fill percentage in the hydrothermal synthesis process to increase catalyst performance for ozone decomposition

The performance of Ce-OMS-2 catalysts was improved by tuning the fill percentage in the hydrothermal synthesis process to increase the oxygen vacancy density. The Ce-OMS-2 samples were prepared with different fill percentages by means of a hydrothermal approach (i.e. 80%, 70%, 50% and 30%). Ce-OMS-2 with 80% fill percentage (Ce-OMS-2-80%) showed ozone conversion of 97%, and a lifetime experiment carried out for more than 20?days showed that the activity of the catalyst still remained satisfactorily high (91%). For Ce-OMS-2-80%, Mn ions in the framework as well as K ions in the tunnel sites were replaced by Ce⁴⁺, while for the others only Mn ions were replaced. O₂-TPD and H₂-TPR measurements proved that the Ce-OMS-2-80% catalyst possessed the greatest number of mobile surface oxygen species. XPS and XAFS showed that increasing the fill percentage can reduce the AOS of Mn and augment the amount of oxygen vacancies. The active sites, which accelerate the elimination of O₃, can be enriched by increasing the oxygen vacancies. These findings indicate that increasing ozone removal can be achieved by tuning the fill percentage in the hydrothermal synthesis process.     

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.