MBBR处理低浓度污水的工程应用

用 2座体积 12 0m3的移动床生物膜反应器处理抚顺乙烯有限公司厂区的低浓度 (CODCr6 0～ 80mg L)生活污水 ,停留时间 2 4h ,出水通过高效纤维球过滤罐 ,CODCr降至 2 0mg L ,BOD5降至 5mg L ,SS降至 5mg L ,氨氮降至 1mg L ,达到了循环冷却水的回用标准。进水浓度过低 ,对MBBR挂膜不利 ,工程中采用外加营养物质的措施后 ,3d内反应器成功挂膜启动。     

地球化学数据去噪方法研究

在简要介绍移动平均、傅立叶交换和小波变换基本原理的基础上，比较了它们在地球化学数据处理过程中去除噪声效果的优劣，并应用于塔北雅克松-轮台地区的地球化学勘探实际。研究结果表明，小波变换是一种理想的数据处理方法。     

微量营养物质对有机废水厌氧消化过程的调控作用

通过向处理酸性葡萄酒蒸馏废水的厌氧移动床生物膜反应器中投加微量营养物质的试验,得出利用微量营养物质调控厌氧消化过程在技术上是可行的。Fe、Ni、Co组合不仅能加快挥发性有机酸(VFA),特别是丙酸的降解速率,进而提高厌氧反应器的溶解COD去除率,同时,还有利于厌氧反应器有机负荷的快速提升和较强pH缓冲能力的形成。B族维生素对厌氧移动床生物膜反应器运行效果影响不大。Fe对厌氧移动床生物膜反应器运行有一定影响,但效果也不十分明显。     

移动床生物膜反应器充氧能力的试验研究

对移动床生物膜反应器的充氧能力进行了试验研究，结果表明：反应器充氧能力在添加填料比无填料时大；在悬浮载体能够均匀流化的填充率范围内，反应器充氧能力随着填充率的增大而增大；当填充率大于可以均匀流化的最大填充率时，反应器的充氧能力略有下降。     

序批式移动床生物膜反应器富集反硝化聚磷菌及其在单污泥系统中的应用

本文介绍了在单污泥系统中选择和富集反硝化聚磷菌的国内外研究进展,对不同研究者提出的选择和富集反硝化聚磷菌的方法进行了分析和评价,并提出将反硝化聚磷菌与移动床生物膜反应器工艺结合起来,在序批式移动床生物膜反应器悬浮填料上选择和富集反硝化聚磷菌,进一步认识了反硝化聚磷菌的生化特征,使其成为反应器中优势菌群,以及该工艺今后的研究重点。     

污水处理移动床生物膜反应器悬浮载体研究进展

介绍了移动床生物膜反应器(MBBR)中悬浮载体的种类和特性,讨论了对其性能的影响因素,总结了当前悬浮载体改性技术及性能评价的方法,并对后续研究提出了建议。     

MBBR处理制药废水的试验研究

采用二级移动床生物膜反应器(MBBR)处理呋喃铵盐制药废水。在填充比为40%,总水力停留时间为32h时,COD的去除率为88.6%,TN的去除率为25.7%,第二级反应器对NH3-N的去除率为56.2%。     

MBBR与A/O法对污水中有机物及氮处理效果的研究

实验在不同水力停留时间（HRT）、进水COD浓度和不同COD容积负荷条件下考察了移动床生物膜反应器（MBBR）和活性污泥A/O工艺对污水中有机物及氮的处理效果。结果表明,MBBR工艺去除有机物和脱氮效果均优于A/O工艺。在进水COD和NH₃－N浓度分别为1000和25 mg/L,HRT为8 h时,MBBR的COD和TN去除率分别为92％和94％,而A/O工艺分别为78％和82％。造成这种结果的原因是MBBR的生物活性高,并且在生物膜内发生了同时硝化反硝化。MBBR脱氮能力受COD冲击明显小于A/O,但在较低进水COD浓度下,两者TN去除率均较低。     

Downward Migration of Dense Bottom Currents

The focus of this paper is on the dynamics of a dense current flowing along the continental slope, and the frictionally induced downward motion it experiences. In particular, the movement of the lateral boundaries where the isopycnals meet the bottom are considered. The current is taken to be wide compared to the Rossby radius, which is in accordance with observations and makes the dynamics quasigeostrophic. The time development of the plume thickness is studied, using three different parameterisations for the bottom friction.Independently of the choice of parameterisation, the following results are obtained: In the central part of the plume friction acts as a diffusive process to minimise the curvature of the upper surface of the plume. At the upper edge the plume quickly approaches a state with small slope, i.e. small geostrophic velocity and small frictionally induced downward flow. At the lower edge a tongue of dense water shoots out creating a widening layer. The thickness of the migrating layer is approximately equal to the boundary layer depth and its downward speed is comparable to the along-slope geostrophic velocity. The downslope end of the migrating layer may form a steep front which requires some precautions in the numerical procedure.     

THE EFFECTS OF A MOVING RAINSTORM ON DIRECT RUNOFF PROPERTIES1

ABSTRACT: The effects of a moving rainstorm on flood runoff characteristics were investigated. A flood hydrograph simulation model called “FH-Model” and a natural watershed were used. A hypothetical rainstorm of 50 years recurrence interval, 75 mm depth, and 4 hours duration was used to show the effects of velocity and direction of the moving rainstorm on the runoff characteristics. Compared with an equivalent stationary rainstorm (ESRS), the peak flow caused by a rainstorm moving in a downstream direction with a speed equal to channel velocity, V, was 27.5 percent higher and the peak flow caused by the same rainstorm moving in an upstream direction was 21.7 percent smaller. These percentages reduced to 10.5 percent and 8.6 percent for storms moving downstream and upstream, respectively, at three times the channel velocity, 3V. There were negligible differences in the time of peak, T_p between runoff caused by storms moving downstream and runoff produced by ESRS. However, T_p for a storm moving upstream at V velocity was 82 percent higher than that produced by ESRS, but was reduced to 27 percent higher when the storm velocity was 3V.