城市污水强化一级处理技术及发展趋势

基于经济与环保的要求，分析了城市污水强化一级处理的适用情况，指出了城市污水强化一级处理的主要工艺方法、特点、处理效果及应用，并提出了城市污水强化一级处理技术的发展趋势。     

雨后入湖溪流磷污染对西湖的影响及其对策

入湖径流是西湖磷的最主要污染源，尤其是暴雨后径流的磷污染最严重，梅雨（2001年）和台风雨后径流的磷净输入为1.77t，约占西湖全年磷总沉积量的42.5%。西湖流域内土壤表土的磷含量约是母土的两倍。西湖流域内土壤表土富磷和暴雨的冲刷和淋溶是导致雨后径流磷浓度提高的主要原因。提出了几种减小和消除径流磷污染的几种方案，通过分析比较，建渠排暴雨后径流水到钱塘江是比较彻底的消除径流磷污染的措施。     

煤气发生站洗冷废水治理研究

研究了以活性炭作为吸附剂处理煤气发生站废水工艺，并摸索出一整套的工艺参数。实验结果表明，采用活性炭吸附工艺使出水水质得到明显改观，硫化物、氰化物和挥发酚的去除效率均达９０％以上，对ＣＯＤｃｒ、氨氮的去除也收到了明显的效果。     

基于厌氧氨氧化和中温亚硝化的可持续生物脱氮工艺

通过介绍厌氧氨氧化技术（ANAMMOX）和亚硝化技术（SHARON）在污水脱氯处理中的原理,着重从工艺特性分析以及控制因数方面介绍SHARON—ANAMMOX联合工艺,并通过与传统工艺的比较,指出SHARON—ANAMMOX联合工艺是可持续性处理工艺。     

新型城市污水脱氮除磷工艺的试验研究与优化设计

提出了一种改进型A2/O脱氮除磷工艺(MAAO),通过工艺试验和活性污泥2D模型对其进行运行和设计优化.结果表明,系统对COD、TN、NH 4-N和TP的平均去除率分别为85.7%、66.8%、97.35%和78.1%;当COD在300mg/L以上时,脱氮除磷效果均较好,可分别达到70%和90%以上.基于试验结果建立的MMAO工艺数学模型仿真效果良好,可对各单元组合进行优化,校核预测不利工况下的工艺运行效果,实现工艺不同工况下的运行参数优化,较好地实现新工艺的机理性优化设计和运行. MMAO稳定运行出水可达到<城镇污水处理厂污染物排放标准>(GB 18918-2002)一级B标准.由于工艺省去内回流,增加厌氧混合液部分超越提供反硝化碳源,使得运行费用明显降低;系统总停留时间比目前传统的以去除有机污染物为主的生物处理工艺略低,该工艺非常适用于对不具有脱氮除磷功能污水厂的改造.     

化学法除磷的试验研究

探讨了含磷废水在添加不同药剂、不同试验条件下的的处理效率;研究表明:石灰法除磷在〔Ca2+/TP〕(摩尔比)为2:1时,pH值控制在10.0左右,TP的去除率达到96%以上;三氯化铁除磷时控制〔Fe3+/TP〕为2:1,pH值为7.0,TP的去除率能达到96%;硫酸亚铁与活性污泥协同除磷效果优于三氯化铁。     

三维电极法处理苯酚废水影响因素研究

根据电解原理,采用自制三维电极反应器对苯酚废水进行处理。在pH值为3,反应时间为120min,电解电压为15V,极板间距为10cm,曝气强度为0.6m3/h反应条件下,苯酚和COD的最大去除率分别为89.1%和83.2%。表明三维电极法适用于处理浓度较高、且有毒性的废水,是快捷、经济、高效的废水处理方法。     

垃圾渗滤液除氨脱氮新工艺初探

通过对渗滤液经矿化垃圾回灌后水质特征的分析及现有除氨脱氮工艺用于渗滤液处理的可行性分析,提出了"多级低氧硝化反硝化+氨缺氧氧化"生物脱氮工艺流程,并阐述了其工艺的处理效果。得出结论:以渗滤液回灌处理出水作为研究对象,在不外加碳源条件下,该工艺可获得92%~99%的氨氮去除率,保证出水氨氮不高于25 mg/L,同时可获得73%~89%的总氮去除率。     

The role of phosphorus in the metabolism of arsenate by a freshwater green alga, Chlorella vulgaris

A freshwater microalga, Chlorella vulgaris, was grown in the presence of varying phosphate concentrations( 10–500 μg/L P) and environmentally realistic concentrations of arsenate(As(Ⅴ))(5–50 μg/L As). Arsenic speciation in the culture medium and total cellular arsenic were measured using AEC-ICP-MS and ICP-DRC-MS, respectively, to determine arsenic biotransformation and uptake in the various phosphorus scenarios. At high phosphate concentration in the culture medium, 100 μg/L P, the uptake and biotransformation of As(Ⅴ) was minimal and dimethylarsonate(DMAs(Ⅴ)) was the dominant metabolite excreted by C. vulgaris, albeit at relatively low concentrations. At common environmental P concentrations, 0–50 μg/L P, the uptake and biotransformation of As(Ⅴ) increased. At these higher As-uptake levels, arsenite(As(Ⅲ)) was the predominant metabolite excreted from the cell. The concentrations of As(Ⅲ) in these low P conditions were much higher than the concentrations of methylated arsenicals observed at the various P concentrations studied. The switchover threshold between the(small) methylation and(large) reduction of As(Ⅴ) occurred around a cellular As concentration of 1 fg/cell. The observed nearly quantitative conversion of As(Ⅴ) to As(Ⅲ) under low phosphate conditions indicates the importance of As(Ⅴ) bio-reduction at common freshwater P concentrations. These findings on the influence of phosphorus on arsenic uptake, accumulation and excretion are discussed in relation to previously published research. The impact that the two scenarios of As(Ⅴ) metabolism, As(Ⅲ) excretion at high As(Ⅴ)-uptake and methylarsenical excretion at low As(Ⅴ)-uptake, have on freshwater arsenic speciation is discussed.     

Effect of organic matter on phosphorus recovery from sewage sludge subjected to microwave hybrid pretreatment

Microwave (MW) hybrid processes are able to disrupt the flocculent structure of complex waste activated sludge, and help promote the recovery of phosphorus as struvite. In this study, to optimize struvite yield, (1) the characteristics of matter released in MW-hybrid treatments were compared, including MW, MW-acid, MW-alkali, MW-H₂O₂, and MW-H₂O₂-alkali. The results showed that selective release of carbon, nitrogen, phosphorus, Ca^2 +, and Mg^2 + achieved by sludge pretreatment using MW-hybrid processes. MW-H₂O₂ is the recommended sludge pretreatment process for phosphorus recovery in the form of struvite. The ratio of Mg^2 +:NH₄⁺-N:PO₄^3 −-P was 1.2:2.9:1 in the supernatant. (2) To clarify the effects of organic matter on struvite recovery, the composition and molecular weight distribution of organic matters were analyzed. Low molecular weight COD was found to facilitate the removal rate of NH₄⁺-N and PO₄³-P via crystallization, and the amorphous struvite crystals (< 1 kDa) from the filtered solutions had high purity. Therefore, the present study reveals the necessity of taking into consideration the interference effect of high molecular weight organic matters during struvite crystallization from sewage sludge.