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

The landfill of municipal solid waste(MSW) could be regarded as denitrification reactor and involved in ammonia nitrogen biological removal process. In this research, the process was applied to municipal solid waste collected in Shanghai, China, which was characterized by high food waste content. The NH4^ removal efficiency in the system of SBR nitrifying reactor followed by fresh and matured landfilled waste layer in series was studied. In the nitrifying reactor, above 90% of NH4^ in leachate was oxidized to NO2^- and NO3^- . Then high concentrated NO2^- and NO3^- were removed in the way of denitrification process in fresh landfilled waste layer. At the same time, degradation of fresh landfilled waste was accelerated. Up to the day 120, 136.5 gC/(kg dry waste) and 17.9 gN/(kg dry waste) were converted from waste layer. It accounted for 50.15 % and 86.89 % of the total carbon and nitrogen content of preliminary fresh waste, which was 4.42 times and 5.17 times higher than that of reference column respectively. After filtering through matured landfilled waste, BOD5 concentration in leachate dropped to below 100 mg/L, which would not affect following nitrification adversely. Because the matured landfilled waste acted as a well methanogenic reactor, 23% of carbon produced accumulatively from fresh landfilled waste degradation was converted into CH4.     

Kinetics of continuous biodegradation of pesticide organic wastewater by activated carbon-activated sludge

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LPWCO method for the treatment of high concentrated organic wastewater

Based on wet air oxidation (WAO) and Fenton reagent, thispaper raises a new low pressure wet catalytic oxidation(LPWCO)which requires low pressure for the treatment of highlyconcentrated and refractory organic wastewater. Compared withgeneral wet air oxidation, the pressure of the treatment(0.1-0.6MPa) is only one of tens to percentage of latter(3.5-10MPa). Inaddition, its temperature is no more than 180℃.Compared withFenton reagent, while H2O2/COD(weight ratio) less than 1.2, theremoval of COD in the treatment is over twenty percents more thanFenton's even the value of COD is more than 14000mg/L. In thispaper, we study the effect factor of COD removal and the mechanismof this treatment. The existence of synergistic effect (catalytic oxidation and carbonization) for COD removal in H2SO4-Fenton reagent system under the condition of applied pressure and heating (0.1-0.6MPa, 104-165℃) was verified. The best condition of this disposal are as follows:H2O2/COD(weight ratio)=0.2-1.0, Fe2+ 0.6×10-3 mol, H2SO4 0.5mol, COD>1×104mg/L, the operating pressure is 0.1-0.6MPa and temperature is 104-165℃. This method suit to dispose the high-concentrated refractory wastewater, especially to the wastewater containing H2SO produced in the manufacture of pesticide, dyestuff and petrochemical works.     

高浓度废水预处理

从分析冲击炼油污水处理的原因出发，阐述了高浓度废水预处理的重要性；重点介绍了三种好氧生物法处理技术；其中ＳＢＲ法由于工程技术日趋成熟，可优先推广应用     

石油亚砜萃取巯基醋酸的研究

对石油亚砜(PSO)萃取巯基醋酸的条件和影响进行了实验研究,确定了石油亚砜通过氢键和巯基醋酸形成的萃合物的组成.为从废水中回收巯基醋酸以及石油硫醚的综合利用提供了依据.     

AT－SS复合颗粒吸附剂的制备和除铅性能研究

通过颗粒吸附剂在含铅溶液中的振荡实验．研究了凹凸棒石粘土（ＡＴ）和钢渣（ＣＳ）、水泥（ＳＮ）、石英砂（ＳＳ）制得的多种复合颗粒吸附剂的除铅性能及制备条件．确定出最佳颗粒吸附剂为ＡＴ－ＳＳ，混合比为５：１，７００℃下焙烧１２０ｍｉｎ．对铅的静态吸附容量高达５００ｍｇ／ｇ以上，动态吸附容量为６０ｍｇ／ｇ．在１．５ｍｌ／ｍｉｎ的流速下，穿透时间为２０ｈ，洗脱回收率为４８．３％．当Ｐｂ进样量为２００ｍｇ／Ｌ时，ＡＴ－ＳＳ吸附剂在２３６倍床体积之内，流出液浓度低于排放标准．     

高级氧化技术机理及在水处理中的应用进展

综述了近年来发展迅速的高级氧化技术，主要包括Fenton法、臭氧氧化法、湿式氧化技术、超临界水氧化法、纳米光催化氧化法电化学催化降解法及超声降解法等。介绍了各种高级氧化技术的基本原理及在废水处理中的应用进展，并对其特点进行了评述。     

有效微生物技术在渗滤液处理中的应用与发展

介绍了有效微生物(EM)的组成、特点及其处理废水的机理;通过与传统的生化法处理垃圾渗滤液的比较,指出了利用EM技术处理垃圾渗滤液的优势,认为该技术不仅能够提高污染物的去除效率,降低污泥产量,而且能够缩短反应器的响应时间;并介绍了EM制剂在国内外的生产情况,对今后EM技术的发展前景提出了展望.     

BOD5测定方法的研究

通过对比实验，对BOD5的测定方法进行研究，探索用氧电极法测定BOD5的可能性和可行性，对其不足之处提出相应的解决措施，使之能更适用于科研、监测教学等方面的需要。     

实施清洁生产方案走可持续发展之路

提高环保意识，加强环保管理，推行清洁生产，开好污水治理设施，重视环保科研，经济效益与环境效益并重，为保护资源做贡献。