阿哈水库叶绿素a时空分布特征及其与藻类、环境因子的关系

为了解阿哈水库叶绿素a(Chl-a)时空分布特征及其与藻类、环境因子的关系,于2012年枯水期至2013年平水期、丰水期对藻类与理化指标进行分层采样.结果表明Chl-a季节变化明显,与藻类生物量季节变化较为一致,而与丰度差别较大,平水期发生甲藻水华,浓度最高(91μg·L~(-1)),枯水期与丰水期相对较低,分别为8μg·L~(-1)与16μg·L~(-1).枯水期与丰水期水体表层Chl-a浓度略高于中、底层,表层光照、溶解氧相对充足,利于藻类生长;平水期表层Chl-a浓度远高于中、底层,易在表层聚集的甲藻水华是主要原因.大坝Chl-a浓度高于库中,这可能是大坝位于金钟河入库口,营养盐高于库中的缘故.相关性分析得出Chl-a与甲藻门呈极显著正相关(R=0.798,P0.01);Chl-a与TP、DO、pH呈极显著正相关(R=0.762,P0.01;R=0.792,P0.01;R=0.658,P0.01),与TN显著正相关(R=0.388,P0.05)与N/P、NO_3~--N显著负相关(R=-0.37,P0.05;R=-0.435,P0.05).逐步回归分析得出DO、TP、N/P为影响阿哈水库Chl-a分布的主要因子.此外热分层以及水温对Chl-a的影响也不容忽视.     

鹤山灰霾期间大气单颗粒气溶胶特征的初步研究

2012年6月9-17日,使用单颗粒气溶胶质谱仪(SPAMS)分析了鹤山大气中单颗粒的特征,共采集到同时含有正负离子谱图的颗粒763350个,其粒径主要集中在0.2～2.0 μm之间,期间发生灰霾的天数为3d.研究结果表明,该地区的大气颗粒物类型主要可分为7种:元素碳(EC)、有机碳(OC)、元素-有机碳混合(ECOC)、大分子有机碳(HMOC)、海盐(Na-K)、富钾颗粒(K-rich)和富铅颗粒(Pb-rich).灰霾天气下,颗粒中的二次成分含量更高,粒径显著增大.各颗粒类型数量浓度均有一定程度的提高,其中,以EC、ECOC和K-rich的增加最为明显.分析结果表明,水稻秸秆的集中焚烧及EC、ECOC和K-rich的老化是形成本次灰霾的重要原因.     

单光子/光电子在线质谱实时分析聚氯乙烯热分解/燃烧产物

实验室研制了低能光电子磁场增强电离(MEPEI)和单光子电离(SPI)复合电离源,该电离源具有电离化合物范围宽、碎片离子少、质谱图简单等优点,结合飞行时间质谱(TOF-MS)实现了聚氯乙烯(PVC)热分解/燃烧产物的在线分析.针对不同的目标化合物,MEPEI/SPI复合电离源通过调节电离区电场强度,可以快速在SPI和SPI-MEPEI之间切换.PVC热分解/燃烧产物中电离能大于光子能量(10.60 eV)的HCl和CO2(12.74 eV、13.77 eV)利用MEPEI模式电离;而烯烃、二氯乙烯、苯系物、氯苯、苯乙烯、茚满及萘系物等可通过SPI-MEPEI复合模式电离.通过实时监测PVC主要燃烧产物的信号强度随温度的变化趋势可推断出,PVC燃烧产物主要是通过两种机制生成:①250～370℃时,PVC发生脱氯及分子内环化反应,产生大量的HCl、苯和萘;②380～510℃时,PVC发生分子间交联反应,生成烷基芳烃,如甲苯和二甲苯/乙苯等.实验结果表明,SPI/SPI-MEPEI复合离子源TOF-MS分析速度快,应用范围广,在在线分析中具有广泛的应用前景.     

Pollutant emission characteristics of rice husk combustion in a vortexing fluidized bed incinerator

Rice husk with high volatile content was burned in a pilot scale vortexing fluidized bed incinerator. The fluidized bed incinerator was constructed of 6 mm stainless steel with 0.45 m in diameter and 5 m in height. The emission characteristics of CO, NO, and SO2 were studied. The effects of operating parameters, such as primary air flow rate, secondary air flow rate, and excess air ratio on the pollutant emissions were also investigated. The results show that a large proportion of combustion occurs at the bed surface and the freeboard zone. The SO2 concentration in the flue gas decreases with increasing excess air ratio, while the NOx concentration shows reverse trend. The flow rate of secondary air has a significant impact on the CO emission. For a fixed primary air flowrate, CO emission decreases with the secondary air flowrate. For a fixed excess air ratio, CO emission decreases with the ratio of secondary to primary air flow. The minimum CO emission of 72 ppm is attained at the operating condition of 40% excess air ratio and 0.6 partition air ratio. The NOx and SO2 concentrations in the flue gas at this condition are 159 and 36 ppm, which conform to the EPA regulation of Taiwan.     

Biodegradation of 2-methylquinoline by Enterobacter aerogenes TJ-D isolated from activated sludge

Bacterial strain Enterobacter aerogenes TJ-D capable of utilizing 2-methylquinoline as the sole carbon and energy source was isolated from acclimated activated sludge under denitrifying conditions. The ability to degrade 2-methylquinoline by E. aerogenes TJ-D was investigated under denitrifying conditions. Under optimal conditions of temperature (35℃) and initial pH 7, 2-methylquinoline of 100 mg/L was degraded within 176 hr. The degradation of 2-methylquinoline by E. aerogenes TJ-D could be well described by the Haldane model (R² > 0.91). During the degradation period of 2-methylquinoline (initial concentration 100 mg/L), nitrate was almost completely consumed (the removal efficiency was 98.5%), while nitrite remained at low concentration (< 0.62 mg/L) during the whole denitrification period. 1,2,3,4-Tetrahydro-2-methylquinoline, 4-ethyl-benzenamine, N-butyl-benzenamine, N-ethyl-benzenamine and 2,6-diethyl-benzenamine were metabolites produced during the degradation. The degradation pathway of 2-methylquinoline by E. aerogenes TJ-D was proposed. 2-Methylquinoline is initially hydroxylated at C-4 to form 2-methyl-4-hydroxy-quinoline, and then forms 2-methyl-4-quinolinol as a result of tautomerism. Hydrogenation of the heterocyclic ring at positions 2 and 3 produces 2,3-dihydro-2-methyl-4-quinolinol. The carbon-carbon bond at position 2 and 3 in the heterocyclic ring may cleave and form 2-ethyl-N-ethyl-benzenamine. Tautomerism may result in the formation of 2,6-diethyl-benzenamine and N-butyl-benzenamine. 4-Ethyl-benzenamine and N-ethyl-benzenamine were produced as a result of losing one ethyl group from the above molecules.     

闽南城市区域空气中挥发性有机物的污染特征

采用美国EPA TO-15的方法,研究了2011年3月份闽南城市区域空气中VOCs的含量及其污染特征。结果表明:1)漳州工业区空气的VOCs浓度为200.5μg/m3,污染较为严重;厦门交通干道VOCs浓度为74.0μg/m3,泉州商住区的VOCs浓度77.1μg/m3,污染较轻。2)漳州工业区采样点TOP5占TVOCs的比例最高,达77.3%;厦门交通干道与泉州商住区两采样点的TOP5占TVOCs的比例相近,分别为64.1%和62.0%。在所有的采样点中出现的TOP5组分比较集中,主要包括甲苯、苯、二氯甲烷、异丙醇、乙酸乙酯、1,1-二氯乙烯、萘等。3)机动车尾气的排放、工业溶剂的挥发和废气排放可能是厦漳泉三地大气VOCs的主要排放源。4)厦漳泉的BTEX主要来源于汽车尾气和汽油挥发;其中厦门和泉州BTEX浓度相比较处在较低污染水平,漳州处在中等水平。     

Effects of physical and chemical characteristics of surface sediments in the formation of shallow lake algae-induced black bloom

Surface sediments are closely related to lake black blooms. The dissolved oxygen （DO） distribution and its penetration depth in surface sediments as well as the migration and transformation of redox sensitive elements such as Fe and S at the sediment-water interface are important factors that could influence the formation of the black bloom. In this study, dredged and undredged sediment cores with different surface properties were used to simulate black blooms in the laboratory. The Micro Profiling System was employed to explore features of the DO and ∑H2S distribution at the sediment-water interface. Physical and chemical characteristics in sediments and pore waters were also analyzed. The results showed that sediment dredging effectively suppressed the black blooms. In the undredged treatment, DO penetration depth was only 50 μm. Fe^2＋ concentrations, ∑H2S concentrations, and ∑H2S production rates were remarkably higher in surface sediments and pore waters compared to control and dredged treatments. Furthermore, depletion of DO and accumulation of Fe^2＋ and ∑H2S in surface sediments and pore waters provided favorable redox environments and necessary material sources for the blooms. The study results proved that physical and chemical characteristics in surface sediments are important factors in the formation of the black bloom, and could provide scientific guidance for emergency treatment and long-term pre-control of black blooms.     

Enhanced photocatalytic activity of quantum-dot-sensitized one-dimensionally-ordered ZnO nanorod photocatalyst

An efficient photocatalyst was fabricated by assembling quantum dots （QDs） onto one-dimensionally-ordered ZnO nanorods, and the photocatalytic properties for Methyl Orange degradation were investigated by scanning electron microscopy, transmission electron microscopy, X-ray diffraction, UV-Vis-NIR absorption spectroscopy and photoluminescence. The results indicate that the catalyst with assembled QDs is more favorable for the degradation than the pristine ZnO nanorods. The QDs with core-shell structure lower the photocatalytic ability due to the higher carder transport barrier of the ZnS shell layer. Besides its degradation efficiency, the photocatalyst has several advantages given that the one-dimensionally-ordered ZnO nanorods have been grown directly on indium tin oxide substrates. The article provides a new method to design an effective and easily recyclable photocatalyst.     

反硝化菌株DA-1的脱氮研究

菌株DA-1被发现能在好氧和厌氧环境中将硝酸盐转化为气态氮。在以NO3-为唯一氮源的条件下研究了碳源、C/N和pH值对菌株DA-1好氧和厌氧反硝化脱氮的影响。结果表明:同等条件下,48 h内菌株DA-1的厌氧脱氮效率高于好氧脱氮率;菌株DA-1能在好氧和厌氧条件下利用乙酸、柠檬酸以及葡萄糖进行细胞增殖和反硝化。在厌氧条件下,三者作为碳源时的反硝化效率分别为(34.04±0.15)%、(22.72±0.32)%和(11.32±0.06)%,均低于好氧条件下的(25.38±0.14)%、(17.52±0.11)%和(8.06±0.01)%。2种条件下均是乙酸为碳源时反硝化效率最高。而丁二酸仅能在厌氧环境中作为电子供体参与反硝化反应。C/N越高越有利于菌株DA-1的厌氧反硝化,当C/N为10时,反硝化效率最高为(35.06±0.19)%。而在好氧条件下,菌株反硝化效率随着C/N的升高,先升高再降低,当C/N为8时,反硝化效率最高;好氧和厌氧脱氮的最适pH值为7.0。体系偏酸或者偏碱都会造成菌株DA-1脱氮效率的降低并出现亚硝酸盐累积。厌氧环境中pH=5.0时累积的亚硝酸盐浓度高达(8.95±2.05)mg/mL。     

磁性多孔陶粒生物膜反应器处理焦化废水的试验研究

以磁性材料为原料,经过特定的工艺处理,对多孔陶瓷进行磁化改性获得磁性多孔载体,并将该载体应用于生物膜反应器中进行焦化废水处理试验。对不同类型的多孔陶粒载体进行对比试验,结果表明:磁性载体生物膜反应器对COD、NH3-N的去除率比普通活性污泥法高出25%³0%,比非载体生物膜反应器高出15%30%,比非载体生物膜反应器高出15%²0%左右。反应器的曝气量为1.5 L/h,曝气时间为10 h/d,温度为2520%左右。反应器的曝气量为1.5 L/h,曝气时间为10 h/d,温度为25³0℃。焦化废水经磁性载体生物膜反应器处理后,上清液中COD,NH3-N的去除率均在90%左右。出水浓度达到国家工业废水排放二级标准(GB18918-2002)。