城市污水生物脱氮除磷机理研究进展

介绍了生物脱氮、除磷的基本原理，综述了国内上关于城市污水脱氮除磷机理方面的研究现状和进展，并对今后开展这方面的研究提出展望 。     

Utilization of Bagasse Energy in Thailand

Bagasse, a biomass fuel, is the waste generated by the sugar-making process from sugar cane. Sugar making is one of the most important agricultural-produce processing industries for developing countries in Southeast Asia, Latin America and Africa. As sugar producing plants need electric power and process steam, co-generation using bagasse as an alternate fuel for petroleum has been in use for some time. Thailand recently became one of the largest sugar exporters by enlarging plant capacities and improving equipment, thus reducing its production cost. In addition, the Thai government promotes power generation using bagasse as a means to combat global warming by raising the purchase price of the surplus power. The industry is in the process of further raising the plant capacity, and improving the power-generating efficiency. This will enable a plant to generate more electric power than its in-plant need so that the surplus power can be sold to the commercial grid. It also plans to become a local power supplier during off-season of sugar making by adding a condensing turbine generator. A typical Thai sugar plant of the latest design generates steam of 4Mpa at the bagasse boiler outlet with the temperature of 400°C at 84% boiler efficiency. With the bagasse LHV of 7,540 kJ/kg and that of fuel oil 41, 840 kJ/kg, and taking 90%as oil-burning boiler efficiency, 5.95 kg of bagasse would replace 1 kg of oil. The Kyoto Mechanism defines CO₂ generation by fuel oil as 2.65 kg per liter. Using 0.85for the specific gravity of fuel oil, the amount of CO₂ generation will be 3.12 kg-CO₂/kg. Therefore, CO₂reduction per ton of bagasse in terms of fuel oil will be: 3.12/5.95 =0.524 kg-CO₂/kg-bagasse. As 1 kg of bagasse generates 2 kg of steam, the CO₂reduction of a 100t/h steam boiler will be112,660 ton/year for an annual operation of4,300 hours, as follows. 0.524 × 100/2 = 26.2 t-CO₂/h, 26.2 × 4,300 =112,660 t-CO₂/year. This revised version was published online in August 2006 with corrections to the Cover Date.     

活性污泥外循环SBR系统循环污泥释磷能力研究

本试验以HAc作为厌氧释磷的碳源有机物，以SBR系统外循环污泥作为研究对象，探索外循环活性污泥的厌氧释磷能力和获取高浓度富磷污水的途径，试验表明：厌氧过程中聚磷菌吸收HAc和释放PO4^3 的分子比为1：1。即吸收2．06mgHAc-COD将诱导1mgP释放，单位时段比污泥的平均释磷速率Vp=6.54.t^0.76，理想的厌氧时间为60－180min，减少循环污泥释磷系统的反应容积可以提高富磷污水磷酸盐的浓度。     

几种海洋微藻对水中三丁基锡化合物的迁移和转化作用

实验表明，在半抑制效应浓度下纤弱角毛藻，扁藻，三角褐指藻对三丁基锡均有瞬时强吸附作用，其后，微藻对三丁基锡的吸收可单室生物积累模型描述，根据模型曲线拟合求出其总吸收饱和浓度和生物排出速常数，微藻对三丁基锡的生物富集因子高达１０＾４－１０＾５，主要取决于高比表面，高分配比和高摄取速率，７２ｈ纤弱角毛藻对三丁基锡的生物降解率在５％左右。     

高锰酸钾与接触氧化协同除锰及硬度对除锰效果的影响

针对日益严重的地表水锰污染，本实验采用高锰酸钾与接触氧化的方法协同除锰；通过调配进水中Ca²⁺、Mg²⁺含量模拟我国不同地区硬度差异显著的地表水，探究水体硬度对锰的去除效果的影响.结果表明：Mn²⁺被高锰酸钾氧化并形成"锰质活性滤膜"，可在停药后实现稳定有效除锰.成熟滤池的除锰效果会显著受到硬度的影响，进水硬度在40、200、400 mg·L^-1及700 mg·L^-1（CaCO₃计）时，接触氧化滤池分别在48、56、64 d及72 d实现稳定除锰，而4根滤柱对Mn²⁺去除的极限浓度分别为1.8、1.7、1.2 mg·L^-1及0.7 mg·L^-1.     

Simultaneous determination of dissolved organic nitrogen, nitrite, nitrate and ammonia using size exclusion chromatography coupled with nitrogen detector

Accurate quantification of dissolved organic nitrogen (DON) has been a challenge due to the cumulative analytical errors in the conventional method via subtracting dissolved inorganic nitrogen species (DIN) from total dissolved nitrogen (TDN). Size exclusion chromatography coupled with an organic nitrogen detector (SEC-OND) has been developed as a direct method for quantification and characterization of DON. However, the applications of SEC-OND method still subject to poor separations between DON and DIN species and unsatisfied N recoveries of macromolecules. In this study, we packed a series of SEC columns with different lengths and resin materials for separation of different N species and designed an independent vacuum ultraviolet (VUV) oxidation device for complete oxidation converting N species to nitrate. To guarantee sufficient N recoveries, the operation conditions were optimized as oxidation time ≥ 30 min, injection mass (sample concentration × injection volume) < 1000 µL × mg-N/L for macromolecular proteins, and neutral pH mobile eluent. The dissolved O₂ concentration in SEC mobile phase determined the upper limit of VUV oxidation at a specific oxidation time. Compared to conventional HW50S column (20 × 250 mm), HW40S column (20 × 350 mm) with mobile phase comprising of 1.5 g/L Na₂HPO₄·2H₂O + 2.5 g/L KH₂PO₄ (pH = 6.85) could achieve a better separation of DON, nitrite, nitrate, and ammonia. When applied to river water, lake water, wastewater effluent, groundwater, and landfill leachate, the SEC-OND method could quantify DON as well as DIN species accurately and conveniently even the DIN/TDN ratio reached 0.98.     

低温条件下生物除磷系统的强化启动和运行

本文通过对比试验对冬季低温条件下生物除磷系统的启动和运行进行了研究，结果表明，低温条件下：(1)温度对生物除磷系统的影响是通过影响有机物的酸化水解而间接产生作用的；(2)通过人工投加HAc使污水中VFA≥80mg／L时，可以顺利启动生物除磷系统；(3)设置独立水解酸化池，可以提高生物除磷效果，在进水COD=150～300mg/L、磷酸盐=5mg／L时，出水磷酸盐≤1mg／L；(4)低温条件下按照水解-外循环ERP-SBR方式运行时，在磷酸盐浓度高达10mg／L的情况下仍能保证出水磷酸盐浓度≤0．5mg／L。     

对厌氧消化中硫化氢毒性控制的探讨

在厌氧消化处理高浓度硫酸盐废水时，不但存在硫酸盐还原菌与产甲烷菌之间发生基质竞争的问题，而且硫酸盐还原菌将硫酸盐还原产生的硫化氢对产甲烷菌产生毒性作用。本文介绍硫化氢对产甲烷菌产生毒性作用的动力学方程，详细分析在厌氧消化条件下硫化氢对产甲烷菌产生毒性作用的机理，重点阐述三种控制硫化氢毒性的方法：气体吹脱法、化学沉淀法和生物除硫法。     

载La(Ⅲ)-和Fe(Ⅲ)-氨基膦酸型螯合树脂对氟吸附性能的比较

研究并比较了载La（Ⅲ）和载Fe（Ⅲ）大孔氨基膦酸型螯合树脂对饮用水中氟离子的吸附特性。氟在载La（Ⅲ）和载Fe（Ⅲ）的螯合树脂上的吸附不随pH的变化而改变,载金属螯合树脂对氟的饱和吸附容量分别为3.78、3.55mg/g,吸附方式符合Freundlich吸附等温式,代表性竞争离子不影响氟在螯合树脂上的吸附。结果表明载Fe（Ⅲ）和载La（Ⅲ）的螯合树脂是一种有前景的饮水氟去除吸附剂。     

Removal of high concentrated ammonia nitrogen from landfill leachate by landfilled waste layer

IntroductionBiologicalremovalofammonia ,i.e.nitrification denitrificationprocesses,isthemosteffectiveandeconomicmethodfortreatingwastewaterwithhighammonianitrogenconcentration ,suchaslandfillleachate .Buttheleachatefrommaturedlandfillischaracterizedwithlowbiodegradablecarbonconcentration .Sothesupplementaryexternalcarbonsourcehastobeaddedtofacilitatedenitrification .Consequently ,theoperationalcostincreases(Carley ,1991) .Thereisnotonlyabundantorganiccarbon ,butalsoagreatdealofanaerobicandfac…