潮土细菌及真菌群落对化肥减量配施有机肥和秸秆的响应

为了研究化肥减量配施有机肥和秸秆对华北麦玉轮作田潮土细菌和真菌群落的影响,在天津市宁河区试验基地开展田间定位施肥试验,采用Illumina高通量测序技术比较了5种施肥模式（单施化肥处理,F;化肥减施处理,FR;化肥减量与秸秆配施处理,FRS;化肥减量与有机肥配施处理,FRO;化肥减量与有机肥和秸秆配施处理,FROS）下土壤细菌及真菌群落的组成、多样性和结构差异,并结合土壤理化性质分析,探究不同施肥处理下驱动细菌和真菌群落变化的关键土壤环境因子.结果表明,FRO处理显著提高了土壤SOM含量.FROS处理的TP含量显著高于FRS处理,增加了13.33%.FRO和FROS处理AP含量较其它处理显著增加,NH₄⁺-N含量显著高于化肥处理（F和FR）.各施肥处理土壤中优势细菌门类均为变形菌门（Proteobacteria）、放线菌门（Actinobacteria）、绿弯菌门（Chloroflexi）和酸杆菌门（Acidobacteria）,优势真菌门类均为子囊菌门（Ascomycota）.在化肥减量配施有机肥（FRO）的基础上添加秸秆（FROS）显著降低了放线菌门（Actinobacteria）的相对丰度.FRS和FROS处理均显著降低了芽单胞菌门（Gemmatimonadetes）的相对丰度.FROS处理显著提高了浮霉菌门（Planctomycetes）和疣微菌门（Verrucomicrobia）的相对丰度.对于真菌群落而言,有机肥（FRO和FROS）的施入显著提高了子囊菌门（Ascomycota）的相对丰度.与FR处理相比,FROS处理显著降低了被孢菌门（Mortierellomycota）和油壶菌门（Olpidiomycota）的相对丰度,且FRS处理同样显著降低了油壶菌门（Olpidiomycota）的相对丰度.FROS处理的细菌群落Shannon多样性指数显著高于F和FR处理,分别增加了1.26%和1.25%,Chao1指数较F处理显著增加了4.51%,细菌Shannon多样性指数与AP和NH₄⁺-N含量显著正相关（P<0.05）.与FR处理相比,FRS、FRO和FROS处理显著降低了真菌群落Shannon多样性指数,分别达到29.85%、24.94%和25.73%,真菌Shannon多样性指数与AP含量显著负相关（P<0.05）.细菌群落结构在FROS处理下显著区别于F、FR和FRO处理,土壤SM、TP、pH和AP是导致细菌群落结构变化的主要驱动因子;真菌群落结构在FRO和FROS处理下显著区别于F和FR处理,真菌群落结构变化主要受土壤TN、AP和TP的驱动.综上所述,添加有机肥和秸秆改变了土壤理化性质,进而改变了土壤细菌和真菌群落组成,土壤真菌对有机物料的敏感程度高于细菌,细菌和真菌群落结构均受到土壤P的调控,在潮土农业耕作中应引起充分重视.     

MnO2/Al2O3催化剂-微气泡臭氧体系催化降解喹啉及其机理

制备了纳米MnO₂,并以Al₂O₃为载体制备了掺杂型MnO₂/Al₂O₃颗粒催化剂.催化剂焙烧温度和时间分别为500℃和4 h、MnO₂质量分数为8%时,催化剂具有最高的臭氧催化氧化活性.SEM分析表明,纳米MnO₂均匀分布于Al₂O₃载体表面.MnO₂/Al₂O₃催化剂的比表面积（BET）为183.22 m²·g^-1,平均孔容为0.27 cm³·g^-1,平均孔径为4.87 nm.建立了MnO₂/Al₂O₃催化剂-微气泡臭氧催化反应体系,研究了该体系对喹啉的降解去除效果及其机理.臭氧微气泡的平均粒径为61.7 μm.微气泡臭氧投量为30 mg·L^-1时,反应60 min后喹啉去除率能达到95%以上;反应20 min后,MnO₂/Al₂O₃催化剂-微气泡臭氧体系对实际煤化工废水二级出水的TOC去除率可达到55%以上.以叔丁醇作为分子探针,证明了羟基自由基（·OH）氧化作用在臭氧微气泡催化氧化体系中对喹啉的降解起到主导作用.     

电场与MnxCey催化剂在苯氧化反应中的协同效应及机理探究

挥发性有机物（VOCs）大量排放已成为日益严重的环境问题,为了实现VOCs的高效去除,本文采用自蔓延燃烧合成法制备了一系列锰铈复合氧化物催化剂,将稳恒直流电场引入典型VOCs气体苯的催化氧化过程,并基于不同电场条件下催化剂的理化性质表征结果进行机理分析.实验结果表明,Mn_xCe_y催化剂对含苯废气的去除有良好的效果,稳恒直流电场显著促进了催化剂的活性,其中Mn₁Ce₃的催化性能最佳,电流为5 mA时,Mn₁Ce₃催化剂在155℃可达到50%的苯转化率,在202.4℃可达到90%的苯转化率,对应的转化温度T₅₀和T₉₀比传统方法分别降低了62.4℃和48.3℃,且电场中的反应活化能由52.32 kJ·mol^-1降低至32.31 kJ·mol^-1.根据实验现象及表征结果,发现协同效应与活性位点的快速持续再生及活性氧物种的转化有关,由此提出苯在Mn_xCe_y催化剂上的氧化机理及电场协同催化的反应模型.     

固定源可凝结颗粒物稀释采样器的设计

固定污染源烟气排放进入大气环境后稀释降温,气相中部分饱和蒸气压较低的组分转化为可凝结颗粒物,这部分颗粒物在固定源烟气颗粒物监测中通常被忽略.为评价固定源可凝结颗粒物的排放情况,本文设计开发并评测了一套稀释采样器.稀释采样器稀释比在10：1~40：1范围内,混合停留时间为5~10 s.实验室评测结果表明,稀释气颗粒物背景值低（（~0.1±0.08） 个·cm^-3）,稀释采样器气密性良好,烟气和稀释气能够均匀混合,颗粒物损失较少,细颗粒物 （PM_2.5）损失在5%以下.本稀释采样器能模拟烟气与环境空气混合降温过程,可用于固定源可凝结颗粒物的测量.     

DOC+CDPF对国III重型柴油货车实际道路排放的影响

利用便携式车载排放测试系统（PEMS）对2辆加装氧化催化转化器（DOC）和催化型柴油颗粒捕集器（CDPF）与否的国III重型柴油货车进行实际道路排放测试.结果表明,2辆改造重型柴油车的CO、THC、固态颗粒物粒数（SPN）和黑碳（BC）实际道路排放因子分别为（1.31±0.37）g/（kW×h）、（0.20±0.03） g/（kW×h）、（7.13×10¹⁰±5.27×10¹⁰）个/（kW×h）和（0.69±0.06）mg/（kW×h）,相对于原始排放（拆除DOC+CDPF）分别降低52.48%、55.69%、99.91%和99.22%.从低速、中速到高速,CO和THC减排比例呈现上升趋势,然而运行工况对SPN和BC减排比例则无显著影响.加装DOC+CDPF会导致NO₂在NO_x中的占比升高,且从低速、中速到高速涨幅依次增大,但对NO_x无明显减排效益,其排放因子为9.53~9.83g/（kW×h）,远高于实验室排放限值.     

Preparation of hydrophobic hierarchical pore carbon–silica composite and its adsorption performance toward volatile organic compounds

Carbon–silica materials with hierarchical pores consisting of micropores and mesopores were prepared by introducing nanocarbon microspheres derived from biomass sugar into silica gel channels in a hydrothermal environment.The physicochemical properties of the materials were characterized by nitrogen physical adsorption(BET),scanning electron microscopy(SEM),and thermogravimetric(TG),and the adsorption properties of various organic waste gases were investigated.The results showed that microporous carbon materials were introduced successfully into the silica gel channels,thus showing the high adsorption capacity of activated carbon in high humidity organic waste gas,and the high stability and mechanical strength of the silica gel.The dynamic adsorption behavior confirmed that the carbon–silica material had excellent adsorption capacity for different volatile organic compounds(VOCs).Furthermore,the carbon–silica material exhibited excellent desorption characteristics:adsorbed toluene was completely desorbed at 150℃,thereby showing superior regeneration characteristics.Both features were attributed to the formation of hierarchical pores.     

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.     

Performance of different macrophytes in the decontamination of and electricity generation from swine wastewater via an integrated constructed wetland-microbial fuel cell process

Plants constitute a major element of constructed wetlands(CWs).In this study,a coupled system comprising an integrated vertical flow CW(IVCW) and a microbial fuel cell(MFC) for swine wastewater tre atment was developed to research the effects of macrophytes commonly employed in CWs,Canna indica,Acorus calamus,and Ipomoea aquatica,on decontamination and electricity production in the system.Because of the different root types and amounts of oxygen released by the roots,the rates of chemical oxygen demand(COD) and ammonium nitrogen(NH_4~+-N) removal from the swine wastewater differed as well.In the unplanted,Canna indica,Acorus calamus,and Ipomoea aquatica systems,the COD removal rates were 80.20%,88.07%,84.70%,and 82.20%,respectively,and the NH_4~+-N removal rates were 49.96%,75.02%,70.25%,and 68.47%,respectively.The decontamination capability of the Canna indica system was better than those of the other systems.The average output voltages were 520±42,715±20,660±27,and 752±26 mV for the unplanted,Canna indica,Acorus calamus,and Ipomoea aquatica systems,respectively,and the maximum power densities were 0.2230,0.4136,0.3614,and0.4964 W/m~3,respectively.Ipomoea aquatica had the largest effect on bioelectricity generation promotion.In addition,electrochemically active bacteria,Geobacter and Desulfuromonas,were detected in the anodic biofilm by high-throughput sequencing analysis,and Comamonas(Proteobacteria),which is widely found in MFCs,was also detected in the anodic biofilm.These results confirmed the important role of plants in IVCW-MFCs.     

Effects of SO2 and H2O on low-temperature NO conversion over F-V2O5-WO3/TiO2 catalysts

F-V_2 O_5-WO3/Ti02 catalysts were prepared by the impregnation method.As the content of F ions increased from 0.00 to 0.35 wt.%,the NO conversion of F-V_2 O_5-WO_3/TiO_2 catalysts initially increased and then decreased.The 0.2 F-V_2 O_5-WO_3/TiO_2 catalyst(0.2 wt.% F ion)exhibited the best denitration(De-NOx) performance,with more than 95% NO conversion in the temperature range 160-360℃,and 99.0% N2 selectivity between 110 and 280℃.The addition of an appropriate amount of F ions eroded the surface morphology of the catalyst and reduced its grain size,thus enhancing the NO conversion at low temperature as well as the sulfur and water resistance of the V_2 O_5-WO3/Ti02 catalyst.After selective catalytic reduction(SCR) reaction in a gas flow containing SO_2 and H_2 O,the number of NH3 adsorption sites,active component content,specific surface area and pore volume decreased to different degrees.Ammonium sulfate species deposited on the catalyst surface,which blocked part of the active sites and reduced the NO conversion performance of the catalyst.On-line thermal regeneration could not completely recover the catalyst activity,although it prolonged the cumulative life of the catalyst.In addition,a mechanism for the effects of S02 and H_2 O on catalyst NO conversion was proposed.     

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.