关于Marpol 73／78附则VI的出台经过及对策

介绍国际海事组织海上环境保护委员会关于Ｍａｒｐｏｌ ７３／７８公约附则ＶＩ的有关焦点问题的讨论情况，该附则Ⅵ业已以议定书形式被外交大会通过。它所涉及的范围较广，技术设备难度大，为贯彻落实该规则尚须在管理上，船舶设备条件等方面下功夫，以满足公约防止船舶对大气污染的要求。     

A／O工艺处理石油化工废水试验研究

本文介绍了采用Ａ／Ｏ新工艺组合处理高浓度的炼油、化工混合废水中试情况，试验结果表明；Ａ／Ｏ新工艺组合具有抗冲击性能好，产泥量少，在一定条件下，出水各项指标达标排放，还就填料选择、含氮化合物的消化反应、污泥生物相和各池工艺参数相互关系进行了讨论。     

某糠醛厂排放废水及周围地下水的GC/MS测定

某地地下水显淡黄色有异味，为查明被污染原因，我们利用ＧＤＸ－１０２树脂富集，对该处唯一的一家工厂——某糠醛厂排放的废水及其周围地下水同时进行了ＧＣ／ＭＳ测定．以上两种水体中均有呋喃类化合物（包括糠醛）及酚类化合物检出，而远离工厂的上游地下水未发现以上两类化合物，这一结果表明，该地下水区被工厂排放的废水所污染     

超声波/Fenton联用对对硝基苯酚的处理

采用超声/Fenton联用技术对水中对硝基苯酚(P-NP)进行处理,探讨了单纯超声(US)、Fenton试剂法、US/Fenton试剂法联用对P-NP的处理效果和影响因素,结果表明,对于浓度为10mg/L的P-NP, 当pH=3、H2O2与Fe2 投加量之比为10:1、H2O2投加量为40mg/L时降解效果最好,通过动力学分析发现US/Fenton试剂法对P-NP的降解具有明显的协同效应.     

银硫离子选择电极测定工业废水中的硫化物

本法用Ag/S离子选择电极测定废水中的硫化物,测定浓度范围0.1～1000.0mg/l,方法精密度为4.3％,回收率为P2.5％,检出限为0.1mg/l。大多数离子不干扰测定,该法简便快速,适用于例行监测。     

Insights into the mechanism of the deterioration of mainstream partial nitritation/anammox under low residual ammonium

Residual ammonium is a critical parameter affecting the stability of mainstream partial nitritation/anammox (PN/A), but the underlying mechanism remains unclear. In this study, mainstream PN/A was established and operated with progressively decreasing residual ammonium. PN/A deteriorated as the residual ammonium decreased to below 5 mg/L, and this was paralleled by a significant loss in anammox activity in situ and an increasing nitrite oxidation rate. Further analysis revealed that the low-ammonium condition directly decreased anammox activity in situ via two distinct mechanisms. First, anammox bacteria were located in the inner layer of the granular sludge, and thus were disadvantageous when competing for ammonium with ammonium-oxidizing bacteria (AOB) in the outer layer. Second, the complete ammonia oxidizer (comammox) was enriched at low residual ammonium concentrations because of its high ammonium affinity. Both AOB and comammox presented kinetic advantages over anammox bacteria. At high residual ammonium concentrations, nitrite-oxidizing bacteria (NOB) were effectively suppressed, even when their maximum activity was high due to competition for nitrite with anammox bacteria. At low residual ammonium concentrations, the decrease in anammox activity in situ led to an increase in nitrite availability for nitrite oxidation, facilitating the activation of NOB despite the dissolved oxygen limitation (0.15–0.35 mg/L) for NOB persisting throughout the operation. Therefore, the deterioration of mainstream PN/A at low residual ammonium was primarily triggered by a decline in anammox activity in situ. This study provides novel insights into the optimized design of mainstream PN/As in engineering applications.     

循环式活性污泥法中厌氧生物选择区的运行条件研究

研究了循环式活性污泥法中厌氧生物选择区的停留时间、进水有机物浓度和系统中泥龄、曝气时间等运行参数对选择区内厌氧释磷以及有机物的吸收贮存的影响。结果表明，选择区停留时间lh，系统泥龄5d，曝气2h，进水有机物浓度COD／TP=60--70，选择器中释磷效果及微生物的吸附性能最优，可去除进水中78％的COD。而且污泥沉降性能良好，试验运行过程中，SVI一直保持在30--40ml／g左右。     

江宁开发区污水处理厂二期调试运行

江宁开发区污水处理厂建设规模为4万m^3／d，分两期建成，采用氧化沟处理工艺，污泥处理采用不经消化的带式脱水工艺。在此主要叙述了各工艺构筑物的设备配置、功能、设计参数及二期工程的试运行情况。     

UV/TiO_2/H_2O_2法对高浓度有机废水降解的应用研究

用UV TiO2 H2 O2 法对高浓度有机废水降解的实验表明 ,当TiO2 、H2 O2 的投加量分别为 2 0g与 1% ,反应时间为3h时 ,CODCr、Oil、Ar OH、NH3 N、S2 - 的平均去除率分别达到 73 %、83 %、86%、5 0 %、10 0 %。此处理工艺具有除臭、除色、快速高效、不产生污泥等优势。实验过程探索了TiO2 、H2 O2 的用量对各污染物降解率的影响 ,并设计了有实用意义的反应器     

Decomplexation of Cu-1-hydroxyethylidene-1,1-diphosphonic acid by a three-dimensional electrolysis system with activated biochar as particle electrodes

The feasibility of decomplexation removal of typical contaminants in electroplating wastewater, complexed Cu(II) with 1-hydroxyethylidene-1,1-diphosphonic acid (Cu-HEDP), was first performed by a three-dimensional electric reactor with activated biochar as particle electrodes. For the case of 50 mg/L Cu-HEDP, Cu(II) removal (90.7%) and PO initial pH 7, acid-treated almond shell biochar (AASB) addition 20 g/L, and reaction time 180 min, with second-order rate constants of 1.10 × 10⁻³ and 1.94 × 10⁻⁵ min⁻¹respectively. The growing chelating effect between Cu(II) and HEDP and the comprehensive actions of adsorptive accumulation, direct and indirect oxidation given by particle electrodes accounted for the enhanced removal of Cu-HEDP, even though the mineralization of HEDP was mainly dependent on anode oxidation. The performance attenuation of AASB particle electrodes was ascribed to the excessive consumption of oxygen-containing functionalities during the reaction, especially acidic carboxylic groups and quinones on particle electrodes, which decreased from 446.74 to 291.48 µmol/g, and 377.55 to 247.71 µmol/g, respectively. Based on the determination of adsorption behavior and indirect electrochemical oxidation mediated by in situ electrogenerated H₂O₂ and reactive oxygen species (e.g., •OH), a possible removal mechanism of Cu-HEDP by three-dimensional electrolysis was further proposed.