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.     

OTC－1型开顶式气室的结构和性能

本文详细论述了开放式气室的结构与性能，二氧化碳浓度数据采集系统、物理性能等。并重点介绍了作者自行研制的ＯＴＣ－Ｉ型开顶式气室。     

H2O2 formation from photocatalytic processes at the ZnO/water interface

The paper focuses on the production of H2O2 by photocatalysis over ZnO in an aerated aqueous phase. The presence of different reductants that increase the H2O2 production in the aqueous phase is analysed; particular attention is paid to nitrite, which has been shown to be the reductant that produces the most significant increments in the H2O2 production. The photocatalytic anodic decomposition of ZnO in the presence of the different reductants is also investigated. From the results obtained, the relevance of the ZnO photocatalysis in the formation of environmental hydrogen peroxide is estimated.     

Ti/Cu交联累托石光催化氧化处理硝基苯废水研究

以钛酸丁酯为钛源,掺杂铜(CuCl2)制备交联剂.制得柱状Ti/Cu交联累托石,结合其吸附特性并通过其在光催化氧化条件下处理含硝基苯有机废水.在pH=9,交联累托石用量为30 g/L,一根20 W紫外灯光辐照2 h的处理条件下,硝基苯由73.81 mg/L降至3.17 mg/L,去除率达到95.71%,优于GB-8978-1996三级标准,用其处理含硝基苯工业废水,COD去除率为83.73%,由4800 mg/L降至530.4 mg/L,硝基苯去除率达92.3l%,由10.32 mg/L降至0.79 mg/L,小于GB-8978-1996-级标准.     

MBBR与A/O法对污水中有机物及氮处理效果的研究

实验在不同水力停留时间（HRT）、进水COD浓度和不同COD容积负荷条件下考察了移动床生物膜反应器（MBBR）和活性污泥A/O工艺对污水中有机物及氮的处理效果。结果表明,MBBR工艺去除有机物和脱氮效果均优于A/O工艺。在进水COD和NH₃－N浓度分别为1000和25 mg/L，HRT为8 h时，MBBR的COD和TN去除率分别为92％和94％，而A/O工艺分别为78％和82％。造成这种结果的原因是MBBR的生物活性高，并且在生物膜内发生了同时硝化反硝化。MBBR脱氮能力受COD冲击明显小于A/O，但在较低进水COD浓度下，两者TN去除率均较低。     

A/O脱氮工艺的控制策略和应用性研究

根据A/O脱氮工艺的运行状况和影响因素 ,提出了应用在线传感器连续测定曝气池中DO浓度、氨氮浓度和硝酸氮浓度 ,并据此调节供氧强度、内循环回流量、有机碳源的投加以及硝化区和反硝化区的大小 ,这是保证A/O脱氮工艺良好处理效果的重要控制策略和思想。同时对近年来国外A/O脱氮工艺自动控制的应用及研究进行了简单的回顾。     

Ce掺杂纳米TiO2光催化剂的制备及降解甲醛的研究

介绍了溶胶-凝胶法制备Ce离子掺杂纳米TiO2的工艺流程.采用X射线衍射(XRD)、紫外可见分光光度法(UV-Vis)等方法表征了Ce掺杂TiO2的相组成、紫外可见漫反射率与掺杂量的关系.结果表明,掺杂的TiO2在520℃、650℃焙烧2 h呈锐钛矿结构,在520℃焙烧2 h的TiO2的晶粒尺寸大约为20 nm,而掺杂Ce后其晶粒尺寸均减小,大约为12nm.UV-Vis吸光度分析表明,掺Ce后吸收带边明显发生红移,但随着Ce掺杂浓度的增大,其对可见光的吸收影响不大.光催化降解反应表明,未掺杂Ce的TiO2反应2 h后对甲醛的没有降解作用,而Ce掺杂TiO2反应2 h后甲醛降解率达15%.     

Dechlorination of 1,2,4-trichlorobenzene in the sediment of Ise Bay

The relation between dechlorination activities of 1,2,4-trichlorobenzene and anaerobic microbial activity were studied in the sediment collected at three sites in Ise Bay in Japan. The degradation rate of spiked 1,2,4-trichlorobenzene (3nmol ml⁻¹) ranged from 15 to 35 pmol day⁻¹ ml⁻¹ wet sediment and about 1/3 to 1/2 of degraded the trichlorobenzene was recovered as dechlorinated products. Among the dichlorobenzenes, the 1,2-isomer had the highest and 1,3-isomer had the lowest production rate. Comparing the three sampling sites, the trichlorobenzene degradation and dichlorobenzenes production rates were related to the sulfate reducing activity for the unit number of sulfate reducing bacteria. Production rates of dichlorobenzenes were completely inhibited by adding molybdate (20 mM), nitrate (60 mM), and formaldehyde solution (4 %). These results indicated that dechlorination activity in the Ise Bay sediment was supported by sulfate reduction activity in the sediment, and not supported by any other anaerobic microbial activity.