抗生素废水的铁屑微电解预处理研究

研究了采用铁屑微电解法预处理抗生素废水.在进水COD质量浓度为6.2 g/L时,试验结果表明,经微电解处理后的废水,COD和色度的去除率分别达到68.3%和79.3%,BOD5/COD从0.306提高到0.56,废水的可生化性得到显著提高.通过正交试验考察pH、反应时间及铁屑用量对处理效果的影响,并对各因素作了单因素影响试验,确定了最佳工艺条件.     

混凝-气浮-加压曝气工艺处理屠宰废水

高浓度生猪屠宰废水属难治理工业废水.采用混凝-气浮-加压曝气工艺处理屠宰废水,经生产实践证明,出水水质可达到<肉类加工工业水污染物排放标准>(GB13457-92)中的一级标准.     

厌氧-Carrousel氧化沟处理亚麻沤制废水的试验研究

亚麻沤制废水是一种高浓度有机废水,经厌氧处理后,出水仍不达标.采用厌氧-Carrousel氧化沟进行后续处理试验,并引进了ACF32微生物制剂进行污泥培养,出水CODCr值在200 mg/L左右,TN值维持在22 mg/L左右,TP值维持在3 mg/L以下,最后讨论了试验中影响处理效果的主要因素.     

改性纤维球处理炼油废水的应用研究

通过用改性纤维球处理炼油废水的试验,对纤维球过滤技术的处理效果和反冲洗特性进行了详细的研究,试验结果表明,炼油废水经处理后,出水中油的含量小于4 mg/L、悬浮物含量小于6 mg/L,出水可达标排放,并且经过改性后的纤维球在含油废水处理中可以通过反冲洗再生并重复使用.     

电解法处理含镍废水及纯镍的回收

采用电解回收法处理Ni2+含量为2g/L的废水,在阴极回收纯镍。研究了电解电流、极距、NH4Cl浓度、pH值等因素对Ni2+去除率、槽压、阴极能耗的影响,得出最优工艺参数为:温度20℃,电解时间20min时、电解电流300mA,极距15mm,NH4Cl浓度5g/L,pH值8.0,该条件下Ni2+去除率为96.926%,槽压16.21V,阴极能耗22.418kW.h/kg,在阴极可得到沉积6.45μm厚的镍板。     

对小纸厂碱回收可行性的初步评价

本文对小型造纸厂的碱回收在技术上和经济上的可行性进行了分析,作出了当前是中、小型造纸厂搞碱回收的有利时机的初步评价。     

新型电极及其电解阳离子染料染色模拟液研究

本文研制了一种可用于废水处理的新型阳极和阴极，研制电极电解处理离子染料色模拟液时，分解电压低，脱色率高，电能消耗少。     

改性脲醛树脂絮凝浮选剂在污水处理中的应用

用尿素和甲醛作为主要原料合成脲醛树脂季胺盐和脲醛树脂叔胺盐。采用ＷＥＭＣＯ浮选模型机和自行设计的模拟现场充气浮选的气浮设备及现场污水对絮凝浮选剂除油、除悬浮物的性能进行了评价。另外，用核磁共振和红外光谱测定了脲醛树脂叔胺盐的结构，并用凝胶色谱法测定了其分子量。     

DOMESTIC WASTEWATER TREATMENT BY PEATLANDS IN A NORTHERN CLIMATE: A WATER QUALITY STUDY1

ABSTRACT: The use of peatlands as the main form of wastewater treatment in a northern climate was studied for the James Bay Energy Society. The Fontanges campsite (70° 17′ 30″ W; 54° 34′ 00″ N) was chosen as the study site. In less than 1.5 km from the point of discharge BOD₅, COD, total hardness, inorganic carbon, orthophosphates, total phosphorus, ammonia and total nitrogen were reduced by at least 90 percent. The peatland treatment system studied is divided into four components, each having a specific function. The first part combines the action of microorganisms and adsorption on peat, thus reducing the organic content while increasing the inorganic constituents. The second part uses peat to adsorb the inorganic elements already present in the wastewater and those produced in the first part of the system. The third component acts as an aerator, increasing the dissolved oxygen and decreasing the BOD₅ levels of the water. The fourth part removes most of the remaining nutrients, thus acting like a tertiary treatment. Overall, peatlands seemed to be effective in treating domestic settled wastewater in a cold climate.     

BIOECONOMIC CONSIDERATIONS FOR WASTEWATER REUSE IN AGRICULTURAL PRODUCTION1

ABSTRACT: Urban wastewater can be a valuable source of water and plant nutrients for agricultural producers, particularly in arid regions. The scientific literature reveals cautious optimism concerning the biological, institutional, and economic viability of irrigating crops with secondary-treated effluent. A derived effluent demand function for agricultural producers near Tucson, Arizona, reveals a potential annual demand of 11,000 acre-feet under present price and proposed delivery system conditions. In this case, wastewater could be exchanged for ground water and both the urban and rural areas would gain.