四种填料滤器处理养鱼废水的硝化性能

为了研究不同填料对海水养殖废水处理的硝化效能,并为生物滤器硝化动力学模型的构建、生物滤器的设计与管理提供基础数据支持,本文在5个化学耗氧量/总氨氮比0、0.8、2、6、12条件下,研究了竹制空心生化球、麦饭石、陶粒和生物滤球等4种填料的生物滤器去除模拟海水养殖废水中化学需氧量和总氨氮,以及生物膜微生物种群结构和数量的变化。结果表明：在低化学需氧量/总氨氮（＜6）条件下麦饭石填料的生物滤器具有最高的化学需氧量和总氨氮去除效能,最高分别可达850和21 g/(m3·d)（化学需氧量/总氨氮=0.8）;竹制空心     

菊花加工厂废水污染调查及生物处理的初步研究

对菊花加工厂废水中的化学污染物和物理性状进行了检测，并在实验室内采用粉末炭活性污泥法对废水进行小规模处理。在实验条件下，ＢＯＤ５去除率达９３％，ＣＯＤｃｒ去除率为８７％，总氮去除率为４７％，总磷去除率为４０％〈总硬度降低５２％，出水的色度，悬浮物，ＰＨ等均达到排放标准。     

糖蜜酒精废液处理过程中生成的微生物蛋白的最佳水解条件研究

通过实验选择复合蛋白酶水解糖蜜酒精废液处理过程中生成的微生物蛋白,并通过正交试验分析得到最佳水解条件为水解酶加入量5.5g/150mL,水解温度65℃,pH值5和水解时间5h。     

厌氧降解和生物接触氧化法处理奥里油废水的实验研究

本文介绍了以奥里油为原料生产重交沥青的生产废水处理工艺,通过实验模拟,探索了该类废水的生物处理效果,并总结出了该废水生物处理启动调试经验.实验证明,用该工艺处理是可行的,厌氧降解处理COD负荷8.7 kg·m-3d-1,平均去除率达35%,好氧处理COD负荷1.87 kg·m-3d-1,平均去除率达69%,生物处理总的COD平均去除率达80%.最终出水达到GB8978-1996二级排放标准.     

Pretreatment of Coke Oven Waste Water with Blast Furnace Sludge Method and Blast Furnace Sludge Plus Scrap Iron Method

Coke oven waste water is respectively pretreated by blast furnace sludge method and blast furnace sludge plus iron scrap method, the effects of pH and the quantity of materials and treatment time on the removal efficiency of COD are analyzed. The results indicate that blast furnace sludge plus iron scrap method is superior to blast furnace sludge method .The treatment time and pH can greatly affect on the removal efficiency of COD using blast furnace sludge plus iron scrap method. The treatment time after 30 minutes and pH have no remarkable effects the removal efficiency of COD using blast furnace sludge method. The removal efficiency of COD increases with the increase of blast furnace sludge and iron scrap, but the increase rate decreases gradually.     

炭化生活污水污泥对酸化红壤的改良效果

从南京市、马鞍山市和丹阳市的3个污水处理厂采集污泥,在500℃下热解制备炭化污泥,测定了污泥和炭化污泥的性质和重金属含量,研究了污泥和炭化污泥对酸性红壤改良效果,并探讨了炭化污泥中重金属的环境风险。结果表明,污泥和炭化污泥中含有一定量的碱,添加炭化污泥可提高红壤的p H和交换性钙、镁和钾含量,降低土壤交换性铝和交换性H+含量。但污泥中大量铵态氮的硝化作用释放质子,抵消了污泥对红壤酸度的改良作用。添加污泥和炭化污泥提高了土壤有机碳、有效磷和速效钾的含量,提高了土壤肥力。污泥炭化后重金属含量有所增加,但大部分重金属的有效态含量下降,说明热解过程可以降低部分有毒重金属的活性。与对照相比,添加炭化污泥会增加土壤中部分重金属有效态含量,特别是有效态锌含量显著增加,因此炭化污泥农业利用存在一定的环境风险。建议将炭化污泥用于酸化的森林红壤的改良。     

UASB处理养猪场废水条件下进水浓度对污泥颗粒化的影响

UASB能够在很高负荷下稳定运行的重要原因在于反应器内形成的厌氧颗粒污泥。该文研究了利用UASB处理猪场废水时进水COD浓度对污泥颗粒化的影响，结果发现：颗粒直径随进水浓度的上升而增高，受传质过程中所能进入颗粒内部的营养量所控制，因此要根据COD去除率的情况适时提高进水浓度，及时地随微生物数量的增加补充营养，促进污泥颗粒化；也可以避免因浓度变化太快引起细菌生长过快，污泥结构松散，沉降性能下降，COD去除率和产气率降低。     

Characterization of Treatment Processes and Mechanisms of COD, Phosphorus and Nitrogen Removal in a Multi-Soil-Layering System

Characteristics of the treatment processes inside a MSL system were investigated by using a laboratory-scale MSL system, which was set up in a D 10 × W 50 × H 73 cm acrylic box enclosing "soil mixture blocks" alternating with permeable zeolite layers. For the study of the treatment processes inside the system, wastewater, with mean concentrations (mg L⁻¹) of COD: 70, T-N: 12, T-P: 0.9, was introduced into the system at a loading rate of 1,000 L m⁻² d⁻¹. Treatment processes in the MSL system were different for the COD, P and N pollutants. Eighty percent of COD was removed in the 1st soil layer among the 6 layers, and the removal rate increased as water moved down and finally reached 90% in the last layer of the system. Phosphorus concentration was lower under the soil mixture layers than under the permeable layers, presumably because P was adsorbed mainly by soil and mixed iron particles. The P concentration in water gradually decreased in the lower layers of the system. The concentration of PO₄^3--P was generally lower in the aerated MSL system than in the non-aerated one. NH₄⁺-N was adsorbed and nitrified in the upper part of the system. The NO₃⁻-N concentration was lower in water under the soil mixture layers than under the permeable layers, indicating that denitrification mainly occurred in the soil mixture layers.     

The effects of nitrogen sludge load and DO on high concentration nitrous nitrifying system

The purpose of this paper is to investigate the impact of nitrogen sludge load and dissolved oxygen(DO) on nitrite nitrification system. The following conclusions have been drawn based on the experimental data and analysis results: 1) The ammonium degradation rate and the nitrous accumulation rate of high concentration nitrous nitrifying system decline with the increase of NH+4-N sludge load. When HRT is less than two days, the ammonium degradation rate rapidly declines to 25%~29% with the increase of NH+4-N sludge load. When HRT is beyond two days, the ammonium rate of the system slowly falls to 50%~60% with the NH+4-N sludge load increased. When HRT is 2.5 days or 3 days, the declined trend of the system nitrous accumulation rate is not obvious with the NH+4-N sludge load increased. When HRT is 5 days, the decrease of nitrous accumulation rate is caused by the adaptation of sludge. So the NH+4-N sludge load of high concentration nitrous accumulation system should not be too high; 2)With the increase of DO, the ammonium degradation of high concentration nitrous nitrifying system is gradually increased. When the DO is less than 0.7 mg/L, it is not conductive to the ammonium degradation. When the DO is higher than 2 mg/L, the oxide of NH+4-N is changed into the increased of NO3-N and the nitrous accumulation rate declined. If the concentration of DO is controlled within 0.7to 1.3 mg/L, the high concentration nitrous nitrifying system can have a good NH+4-N degradation rate and nitrous accumulation rate.