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.     

深圳市秋季大气臭氧立体分布特征

利用大气O₃探测激光雷达在深圳市东部生态区和西部城区同步开展垂直观测,探究了2018年深圳市O₃立体分布在秋季光化学污染活跃期至冬季非活跃期的演变过程.结果表明：光化学反应活跃的10月,东部地面O₃浓度相对于西部地面高出约128%;地面向上至450m,O₃浓度在东部生态区发生快速降低,而在西部城区由于存在“滴定效应”,O₃浓度随高度升高而升高;450m~2km,东、西部O₃浓度均随高度升高而降低,西部城区O₃浓度水平超过东部生态区约30%;2km以上高空,东、西部O₃浓度趋同（70μg/m³）,并保持稳定,为具深圳市秋季O₃污染过程提供了较高的大气背景浓度.高污染期间,深圳市大气边界层内O₃浓度变化较为一致,西部高空的O₃区域传输作用更加显著.秋季至冬季光化学反应逐渐减弱,深圳市O₃浓度的水平和垂直空间差异逐渐减小,冬季的深圳市O₃污染基本受大气背景控制.     

核壳结构KNbO3@Co(OH)2的制备及其活化过一硫酸盐降解帕珠沙星的研究

制备了以KNbO₃为载体材料的Co（OH）₂复合材料并对其进行了详细的表征,分析了材料的组成成分、组成形态进而确定了其为核壳结构形貌的KNbO₃@Co（OH）₂.利用合成的样品作为催化剂活化过一硫酸盐（peroxymonosulfate,PMS）来降解帕珠沙星（pazufloxacin,PZF）,结果表明制备的催化剂对PZF的去除效率显著增加.讨论了不同初始PMS剂量对降解效率的影响,发现随着PMS增加可活化生成更多的硫酸根自由基（sulfate radicals,SO₄^·-）和羟基自由基（hydroxyl radicals,HO^·）来降解PZF,但继续增大PMS用量降解效率未见明显提升.酸性和中性pH值条件下利于反应活化PMS降解PZF,而碱性体系减缓反应,甚至强碱体系更易形成Co（OH）₂沉淀不利于反应体系中活性组分CoOH⁺的形成,大大抑制了催化性能.此外,在体系中加入淬灭剂叔丁醇（tert-Butanol,TBA）或者乙醇（ethanol,ETOH）进行自由基的淬灭实验,结果表明SO₄^·-自由基为体系降解PZF过程中主要贡献的自由基,而HO^·自由基的贡献较少.催化剂具有较好的稳定性5次循环之后仍能在10 min之内完全去除PZF.本研究提出了新的思路为制备其他载体的Co（OH）₂核壳结构提供参考依据,同时将该催化剂结合高级氧化技术应用到水体新兴有机污染物净化领域具有很好的应用前景.     

Pt-Sn/Al2O3蜂窝催化剂催化氧化C6烃

采用等体积分浸法制备Pt-Sn/Al₂O₃蜂窝催化剂（Pt含量仅为0.06wt%）.运用X射线衍射（XRD）、透射电镜（TEM）等技术对催化剂理化性质进行表征,并选取4种代表性C₆烃（苯、环己酮、环己烷和正己烷）对催化剂性能进行评价.活性评价试验中,Pt/Sn比为3/1催化效果最佳.此时4种C₆烃转化率达到90%的温度（T₉₀）较Pt催化剂均降低约20℃,其原因在于Sn可将Pt分割为较小的团簇提高Pt分散度.寿命评价试验以环己烷为例同Pt-Sn蜂窝催化剂连续运行720h,催化活性无明显变化,其原因在于,Sn可有效抑制其粒径增长;Pt₃Sn合金降低表面对C₆烃的吸附,减少催化剂表面积炭.     

Phosphate recovery with granular acid-activated neutralized red mud: Fixed-bed column performance and breakthrough curve modelling

Granular acid-activated neutralized red mud (AaN-RM) has been successfully prepared with good chemical stability and physical strength. However, its potential for industrial application remains unknown. Therefore, the performance of granular AaN-RM for phosphate recovery in a fixed-bed column was investigated. The results demonstrated that the phosphate adsorption performance of granular AaN-RM in a fixed-bed column was affected by various operational parameters, such as the bed depth, flow rate, initial solution pH and initial phosphate concentration. With the optimal empty-bed contact time (EBCT) of 24.27 min, the number of processed bed volumes and the phosphate adsorption capacity reached 496.95 and 84.80 mg/g, respectively. Then, the saturated fixed-bed column could be effectively regenerated with a 0.5 mol/L HCl solution. The desorption efficiency remained as high as 83.45% with a low weight loss of 3.57% in the fifth regeneration cycle. In addition, breakthrough curve modelling showed that a 5-9-1 feed-forward artificial neural network (ANN) could be effectively applied for the optimization of the fixed-bed adsorption system; the coefficient of determination (R²) and the root mean square error (RMSE) evaluated on the validation-testing data were 0.9987 and 0.0183, respectively. Therefore, granular AaN-RM fixed-bed adsorption exhibits promising potential for phosphate removal and recovery from polluted water.     

Cytotoxicity of the soluble and insoluble fractions of atmospheric fine particulate matter

Inhaled atmospheric fine particulate matter(PM_(2.5)) includes soluble and insoluble fractions,and each fraction can interact with cells and cause adverse effects.PM_(2.5) samples were collected in Jinan,China,and the soluble and insoluble fractions were separated.According to physiochemical characterization,the soluble fraction mainly contains watersoluble ions and organic acids,and the insoluble fraction mainly contains kaolinite,calcium carbonate and some organic carbon.The interaction between PM_(2.5) and model cell membranes was examined with a quartz crystal microbalance with dissipation(QCM-D) to quantify PM_(2.5) attachment on membranes and membrane disruption.The cytotoxicity of the total PM_(2.5) and the soluble and insoluble fractions,was investigated.Negatively charged PM_(2.5) can adhere to the positively charged membranes and disrupt them.PM_(2.5)also adheres to negatively charged membranes but does not cause membrane rupture.Therefore,electrostatic repulsion does not prevent PM_(2.5) attachment,but electrostatic attraction induces remarkable membrane rupture.The human lung epithelial cell line A549 was used for cytotoxicity assessment.The detected membrane leakage,cellular swelling and blebbing indicated a cell necrosis process.Moreover,the insoluble PM_(2.5) fraction caused a higher cell mortality and more serious cell membrane damage than the soluble fraction.The levels of reactive oxygen species(ROS) enhanced by the two fractions were not significantly different.The findings provide more information to better understand the mechanism of PM_(2.5) cytotoxicity and the effect of PM_(2.5) solubility on cytotoxicity.     

Synergistic effects of Cu species and acidity of Cu-ZSM-5 on catalytic performance for selective catalytic oxidation of n-butylamine

In this work, a series of Cu-ZSM-5 catalysts with different SiO₂/Al₂O₃ ratios (25, 50, 100 and 200) were synthesized and investigated in n-butylamine catalytic degradation. The n-butylamine can be completely catalytic degradation at 350°C over all Cu-ZSM-5 catalysts. Moreover, Cu-ZSM-5 (25) exhibited the highest selectivity to N₂, exceeding 90% at 350°C. These samples were investigated in detail by several characterizations to illuminate the dependence of the catalytic performance on redox properties, Cu species, and acidity. The characterization results proved that the redox properties and chemisorption oxygen primarily affect n-butylamine conversion. N₂ selectivity was impacted by the Brønsted acidity and the isolated Cu²⁺ species. Meanwhile, the surface acid sites over Cu-ZSM-5 catalysts could influence the formation of Cu species. Furthermore, in situ diffuse reflectance infrared Fourier transform spectra was adopted to explore the reaction mechanism. The Cu-ZSM-5 catalysts are the most prospective catalysts for nitrogen-containing volatile organic compounds removal, and the results in this study could provide new insights into catalysts design for VOC catalytic oxidation.     

杭州湾北岸上海段石化集中区臭氧重污染过程研究

为研究杭州湾O₃污染的形成机制,采用在线监测系统对杭州湾北岸上海段石化集中区O₃及其前体物开展了为期1个月(2019年5月)的同步连续观测.采用OZIPR(臭氧等值线研究)模型分析O₃生成的敏感性.在O₃重度污染期间,利用PMF(正定矩阵因子分解)模型对O₃前体物——VOCs进行源解析,采用臭氧生成潜势及气团老化分别估算了VOCs的反应活性和化学消耗.结果表明:①2019年5月杭州湾北岸上海段石化集中区O₃的IAQI(空气质量分指数)优良率仅为61.3%,ρ(O₃)第90%分位值为173.0 μg/m3.5月22日、23日发生重度O₃污染,O₃日最大8 h滑动平均值分别为(284.4±19.2)(282.0±14.2)μg/m3,分别超过GB 3095—2012《环境空气质量标准》二级标准限值(160 μg/m3)的77.75%和76.25%.②O₃的生成受VOCs控制,降低VOCs的排放可在一定程度上降低O₃的生成,降低NO_x的排放反而会促进O₃的生成.③O₃重度污染期间,VOCs主要来自化工区排放(72.35%)和机动车尾气排放(27.65%).④O₃重度污染期间,烯烃、炔烃及芳香烃对O₃生成的贡献率之和在80.00%以上,其中丙烯、乙烯和甲苯的贡献率分别为29.97%、15.60%和14.16%;芳香烃及烯烃和炔烃是最主要的VOCs化学消耗物种,其中φ(丙烯)、φ(乙烯)和φ(1,2,4-三甲苯)的消耗量分别为13.57×10-9、4.93×10-9和3.55×10-9.研究显示,杭州湾北岸上海段5月O₃的生成受化工区影响显著,丙烯与乙烯是O₃重污染期间关键的O₃前体物.      

秸秆还田方式对东北农田土壤NH3挥发和N2O排放的影响

秸秆还田是有效利用资源、增加土壤有机质含量和培肥地力的有效措施,但也会影响土壤NH₃挥发和N₂O的排放.探索不同秸秆还田方式对NH₃挥发和N₂O排放的影响对于减少土壤氮素损失和保护生态环境具有重要意义.采用田间小区试验,利用Los Gatos Research（LGR）超便携NH₃分析仪和密闭式静态箱-气相色谱法探究不同秸秆还田方式下土壤NH₃挥发和N₂O排放的特征,试验设4个处理（覆盖还田,即表面覆盖玉米秸秆,0~20和20~40 cm土壤分层扰动后填回,记为JG0-0;常规还田,即秸秆与0~20 cm土壤混合,20~40 cm土壤扰动后填回,记为JG0-20;深还田,秸秆与20~40 cm土壤混合,0~20 cm土壤挖出后填回,记为JG20-40;对照处理,即无玉米秸秆还田,0~20和20~40 cm土壤分层扰动后填回,记为CK）.结果表明:①相比于CK,不同秸秆还田方式均显著降低了土壤NH₃挥发量,增加了土壤N₂O排放量.与CK相比,JG0-0、JG0-20和JG20-40处理下土壤NH₃累积排放量分别减少了12.38%、9.87%和5.73%;土壤N₂O累积排放量分别增加了30.19%、82.82%和36.53%,其中JG0-0和JG20-40处理之间无显著性差异.②JG20-40处理下玉米产量显著高于其他处理,比CK增加了23.15%,JG0-0处理下玉米产量高于CK和JG0-20处理,但并未达到显著水平.③对于NH₃和N₂O这两种气体的总累积排放量,各处理间均达到显著性差异.与CK相比,JG0-0、JG0-20和JG20-40处理下NH₃和N₂O总累积排放量分别增加了16.67%、52.08%和22.92%.④不同秸秆还田方式下的氮素气态损失率均高于CK,JG0-0、JG0-20和JG20-40处理下氮素气态损失率分别比CK增加了17.50%、52.50%和22.50%.因此,综合考虑土壤NH₃挥发量、N₂O排放量和玉米产量等因素,JG0-0处理优于JG20-40、JG0-20处理.      

铁碳促进O3/H2O2体系深度处理准好氧矿化垃圾床渗滤液尾水中难降解有机物

构建了铁碳-O_3/H_2O_2体系降解矿化垃圾床渗滤液尾水中有机物,并考察了体系O_3、铁碳及H_2O_2投加量、初始pH值和反应时间对铁碳-O_3/H_2O_2体系处理渗滤液尾水的影响.结果表明,在铁碳投加量为3 g·L~(-1),O_3投加量为9.798 mg·min~(-1),H_2O_2投加量为2 mL·L~(-1),初始pH值为3的条件下,反应10 min后,渗滤液尾水的COD和UV_(245)分别从711.96 mg·L~(-1)、0.19下降至295.04 mg·L~(-1)、0.10.类比实验结果表明,铁碳-O_3/H_2O_2体系对渗滤液尾水有机物具有较高的去除率,且可生化性得到提高(BOD/COD从0.04增加至0.40).紫外-可见和三维荧光光谱显示,废水中难降解有机物转化为小分子有机化合物且腐殖质的分子缩合度降低.最后,采用SEM-EDS、XRD和XPS技术对铁碳-O_3/H_2O_2体系的反应机理进行了解析,发现铁碳-O_3/H_2O_2反应的机理为铁碳微电解反应、铁氧化物-H_2O_2非均相芬顿反应、O_3/H_2O_2、铁碳-O_3非均相的高级氧化作用和铁基胶体对有机物的吸附沉淀作用.研究表明,铁碳-O_3/H_2O_2体系是一种能够有效去除矿化垃圾床渗滤液尾水中难降解有机物的方法.