Two-site kinetic modeling of bacteriophages transport through columns of saturated dune sand

Breakthrough curves, on a semi-log scale, from tests in porous media with block-input of viruses, bacteria, protozoa and colloidal particles often exhibit a typical skewness: a rather slowly rising limb and a smooth transition of a declining limb to a very long tail. One-site kinetic models fail to fit the rising and declining limbs together with the tail satisfactorily. Inclusion of an equilibrium adsorption site does not seem to improve simulation results. This was encountered in the simulation of breakthrough curves from a recent field study on the removal of bacteriophages MS2 and PRD1 by passage through dune sand. In the present study, results of laboratory experiments for the study of this issue are presented. Breakthrough curves of salt and bacteriophages MS2, PRDI, and phiX174 in 1 D column experiments have been measured. One- and two-site kinetic models have been applied to fit and predict breakthrough curves from column experiments. The two-site model fitted all breakthrough curves very satisfactorily, accounting for the skewness of the rising limb as well as for the smooth transition of the declining limb to the tail of the breakthrough curve. The one-site model does not follow the curvature of the breakthrough tail, leading to an overestimation of the inactivation rate coefficient for attached viruses. Interaction with kinetic site 1 is characterized by relatively fast attachment and slow detachment, whereas attachment to and detachment from kinetic site 2 is fast. Inactivation of viruses and interaction with kinetic site 2 provide only a minor contribution to removal. Virus removal is mainly determined by the attachment to site 1. Bacteriophage phiX174 attached more than MS2 and PRD1, which can be explained by the greater electrostatic repulsion that MS2 and PRD1 experience compared to the less negatively charged phiX174.     

Isomer distribution of nitrotriphenylenes in airborne particles, diesel exhaust particles, and the products of gas-phase radical-initiated nitration of triphenylene

The formation of mutagenic nitro-polycyclic aromatic hydrocarbons (NPAHs) 1- and 2-nitrotriphenylene (1- and 2-NTP) via gas-phase OH or NO₃ radical-initiated reactions of triphenylene was demonstrated for the first time using a flow reaction system. In contrast with the results of conventional electrophilic nitration, 2-NTP was formed in larger yield than 1-NTP, but this is consistent with the mechanism proposed for gas-phase radical-initiated nitration of PAH. In diesel exhaust particle (DEP) samples, both 1- and 2-NTP were identified and their concentrations determined, as well as 1-nitropyrene (1-NP), which is a representative combustion-derived NPAH: the mean concentrations of 1-NTP, 2-NTP, and 1-NP were 4.7, 1.9, and 32 pmol mg_DEP^–1, respectively. The mean 2-NTP/1-NTP, 1-NTP/1-NP, and 2-NTP/1-NP ratios in samples of airborne particles collected in a residential area in Osaka, Japan, were>1.55,<0.25, and 0.37, respectively; these values are much higher than those of the DEP samples. This finding indicates that there is another source for airborne NTPs, especially 2-NTP, apart from diesel exhaust. These results strongly suggest that airborne NTPs originate from atmospheric processes such as radical-initiated reactions of triphenylene, and this has a significant influence on the atmospheric occurrence of NTPs.     

二步法腈纶生产废水的处理试验

本试验采用混凝 -A/O系统组合工艺处理二步法腈纶废水 ,该系统处理效果良好 ,出水水质符合排放标准 ,可直接排入水体。A/O系统试验装置总容积 80L ,水力停留时间 5 8— 70h ,缺氧池与好氧池的容积比为 1∶3 ,回流比 ( 2—3 )∶1,COD和BOD总去除率分别约为 84%和 98%。     

一种新型复合球填料在低浓度污水再生回用中的应用研究

新型复合球填料为沸石与悬浮球填料的有机组合体,密度约为0.92～0.97g/cm3,比表面积为711～1185m2/m3,表面粗糙,物化性能稳定.在曝气量为20∶1,停留时间为6 h时,装有新型复合球填料的反应柱挂膜容易,成膜时间短,膜不易脱落,且生物相丰富.膜成熟时对生活污水中的氨氮和COD都有很好的去除效果,出水氨氮浓度≤2 mg/L,去除率≥93%;出水COD浓度≤22 mg/L,去除率≥80%.新型复合球反应柱在稳定状态处理低浓度的二级出水时,出水氨氮浓度≤2 mg/L,去除率≥89%,出水COD浓度为10～36 mg/L,去除率为48%～81%.出水水质符合GB50335-2002标准.     

生物膜与A／O工艺耦合快速降解氨氮

应用由城市污水处理厂序批式间歇反应器（SBR）中筛选得到的4株特殊氨氧化菌，分别在SBR和有回流的生物膜与A／O工艺耦合体系培养中，考察其降解低碳高氨氮废水的功能。结果表明，自养硝化与异养氨氧化菌的混合菌群较单一自养硝化菌株降解氨氮速率快；在生物膜与A／O工艺耦合系统中，自养硝化与异养氨氧化菌协同代谢加速氨氮氧化脱除，氨氮脱除速率远比SBR系统快。对生物膜与A／O工艺耦合系统中氨氮脱除动力学进行了研究，模拟了NH4^＋、NO2^-；质量浓度与氨氮脱除比速率之间的关系，模型得到了较好的验证。     

光助Ce-Fe/Al2O3催化H2O2降解阳离子红GTL模拟废水

利用Ce-Fe/Al₂O₃为催化剂的非均相光Fenton体系降解阳离子红GTL模拟废水，考察了H₂O₂浓度、催化剂用量、初始pH值及不同工艺过程对降解效果的影响，通过紫外-可见漫反射光谱、红外光谱、XPS手段研究铁在反应中的价态变化。结果表明，在11 W低压汞灯照射下，非均相光Fenton体系能够有效地降解结构稳定的阳离子红GTL，在pH 6，反应温度20℃，时间90 min，Ce-Fe/Al₂O₃ 2 g/L，H₂O₂浓度340 mg/L，含50 mg/L阳离子红GTL模拟废水TOC去除率为92.40%；光Fenton反应中Fe(Ⅲ)转化为Fe(Ⅱ)。     

倒置A2/O污水处理工艺的特点及应用实例

传统A²/O工艺在保证脱氮效果的同时除磷效果往往不佳。在充分分析传统A²/O工艺的基础上，提出了将缺氧池置于厌氧池前面，厌氧池后设置好氧池的分点进水倒置A²/O工艺。某污水厂的现场试验表明，在COD去除能力与常规A²/O工艺相当的情况下，倒置A²/O工艺的脱氮除磷功能明显优于常规A²/O工艺。     

Study of oil-water partitioning of a chemical dispersant using an acute bioassay with marine crustaceans

The toxicity of seawater dispersions of a chemical dispersant to two marine crustaceans was investigated in the presence and absence of various quantities of a non-toxic mineral oil. From the results and a physical-chemical partitioning analysis, a limiting value of the oil-water partition coefficient of the toxic compounds is deduced suggesting that essentially all of the toxic compounds in the dispersant will partition into solution in water following dispersant application to an oil spill. This conclusion simplifies interpretation and prediction of the toxic effects of a dispersed oil spill.The combined bioassay-partitioning procedure may have applications to the study of the toxicity of other complex mixtures such as industrial effluents.     

A/O工艺处理城市生活工业综合污水的耐受性研究

针对目前城市污水处理厂进水水质以生活污水为主转向以难生物处理的工业废水为主的现状,进行了A/O工艺的耐受性试验.结果表明:随着工业废水比例的增加,厌氧、好氧污泥活性都显著下降,厌氧污泥的耐受性较高;随着运行时间的延长,两类污泥的活性逐步得到不同程度的恢复;工业废水比例越高,活性恢复所需时间越长;两类污泥的协同代谢作用保证了出水效果.A/O工艺所能耐受的进水中制药废水、印染废水和生活污水的分配比(体积比)为3∶3∶4.