高浓度氨氮废水好氧反硝化反应的基本条件

文章通过室内实验,对高浓度氨氮废水(垃圾渗滤液)间歇曝气,在只存在有机碳、无机氮的条件下进行好氧反硝化脱氮研究。实验结果表明:垃圾渗滤液中存在好氧反硝化土著微生物菌落;发生好氧反硝化的基本条件为在溶解氧充足的条件下间歇曝气;碳源不仅是厌氧反硝化所必须的,同样也是好氧反硝化的必要条件。     

短程硝化反硝化生物脱氮的实现途径

短程硝化反硝化是近年来开发的一项新的生物脱氮技术,它具有节约曝气量、节省有机碳源和减少污泥产量等优点,实现短程硝化反硝化生物脱氮技术的关键就是将硝化控制在亚硝酸阶段,阻止亚硝酸盐的进一步氧化。简要介绍了短程硝化反硝化生物脱氮技术的原理和技术特点,通过对短程硝化反硝化影响因素的分析来介绍其实现途径,阐述了温度控制途径、溶解氧控制途径、pH值控制途径、投加抑制剂途径、泥龄控制途径以及纯种分离与固定化技术途径的控制机理及其局限性,并提出了今后的研究方向。     

潜流型人工湿地实现短程硝化反硝化的探讨

从短程硝化反硝化机理和目前国内外在短程硝化生物脱氮技术方面的进展入手;介绍了影响短程硝化的因素,剖析了潜流型人工湿地系统实现短程硝化的可能性和可行性;最后展望了湿地系统作为生态处理方法的发展方向.     

短程硝化--反硝化生物脱氮工艺的研究进展

短程硝化反硝化生物脱氮工艺是将硝化控制在形成亚硝酸阶段,阻止亚硝酸的进一步硝化,然后直接进行反硝化。本文结合国内外的研究,对短程硝化脱氮技术的实现途径进行了概括和探讨,对该工艺的开发应用（如SHARON工艺、OLAND工艺、CANONT艺和生物膜／活性污泥法结合的短程硝化反硝化工艺）作了简要综述,并指出了该工艺的技术优势和应用价值。     

新型填料在生物接触氧化工艺中的应用研究

以处理120L／d城镇生活污水的生物接触氧化小试装置为研究平台,介绍了新型内置悬浮球形填料一生物接触氧化工艺的特点及运行状况。试验结果表明：两种新型内置悬浮球形填料对反应器充氧效率、接种挂膜速率、污水处理效果对比均为纤维束状填料好于筒状填料;与连续曝气相比,采用间歇曝气的运行方式,在使出水NH3-N达标的基础上,提高了TN和TP的去除率,系统的同步硝化反硝化现象和反硝化除磷现象比较明显,具有较强的经济性和实用性。     

澳大利亚开发新的水处理技术

一、生活污水处理方法 　　1. AAA污水处理方法 　　这是一种间断性曝气的生物处理过程,通过好氧过程和厌氧过程的交变来消解水中污染物。 AAA是一种带澄清槽和污泥循环的活性污泥系统,连续进、出水,通过传感器检测污水中溶解氧浓度的变化速率来动态地控制曝气量和曝气时间,从而发生硝化和反硝化生物脱氮反应。特点是：曝气能量最小,可连续地控制使 BOD和氮得到最优化地去除,出水中悬浮污泥少,有溶解氧传感器的失灵报警。用 AAA对现有工艺进行改进,可降低成本。 　　2. APT预发酵生物除磷和氮 　　APT是 Activated Primar…     

污水处理厂短程硝化影响因素分析及效果评估

文章基于采用厌氧-缺氧-好氧法(A²O)工艺在某城市污水处理厂形成的稳定短程硝化现象，分析了不同影响因素与短程硝化形成的关联性，评估了实现短程硝化对于该厂能耗、药耗及污染物去除效果的实际影响。     

多孔颗粒载体-膜生物反应器脱氮效果研究

实验探索了高MLSS(溶液悬浮固体浓度)下多孔颗粒载体—膜生物反应器发生短程硝化、反硝化的可能性。研究了溶解氧(DO)、C/N、氨浓度及氨负荷、pH等因素对短程硝化、反硝化和TN去除的影响。实验发现,当控制pH=7.5、DO=1.0mg/L、C/N为6时,该反应器能同时达到较高的NH4 —N和TN出除率。     

短程硝化-反硝化生物脱氮技术研究

将短程硝化-反硝化生物脱氮技术与传统生物脱氮技术进行了比较,论述了短程硝化-反硝化生物脱氮技术的机理及特点。分析了实现亚硝酸盐积累的影响因素,包括温度、溶解氧浓度、pH值、分子态游离NH3浓度和泥龄。结合典型工艺,提出了目前短程硝化-反硝化脱氮技术存在的问题及改进建议。     

低负荷状态下CAST工艺脱氮特性的研究

在征润洲污水处理厂CAST工艺处理城市污水运行实践的基础上,开展了两个阶段的对比生产性试验;对城市污水处理过程中,低负荷运行状态下CAST工艺脱氮特性进行研究。研究结果表明:通过对F/M、DO、MLSS、SRT等工艺参数的优化控制,可实现同步硝化反硝化、短程硝化反硝化和传统硝化反硝化有机结合的耦合脱氮模式。该耦合脱氮模式下各出水水质指标稳定达标的情况下,出水NH3-N的去除率达到90%以上,出水TN去除率在55%以上,取得了良好的脱氮效果。     

OPTIMAL ALLOCATION OF ARTIFICIAL AERATION ALONG A POLLUTED STREAM USING DYNAMIC PROGRAMMING1

ABSTRACT: When a series of aerators are used to raise the level of dissolved oxygen in a polluted stream through instream artificial aeration augmentation, the system is governed by the basic dissolved oxygen mass balance equation with the existence of artificial aeration as its boundary conditions. A mathematical model is formulated for the optimization of the allocation of aeration capacity to each of the series of aerators subject to a limitation on total available aeration capacity. The objective function is the minimization of the sum of the squares of the aeration costs and the costs incurred by damaging or unnecessarily improving the system. The original constrained allocation problem is simplified by converting it to an unconstrained one via the use of Lagrange multiplier. A discretized dynamic programming algorithm is formulated for finding the optimal allocation policy. A typical optimal aeration capacity allocation policy and its corresponding dissolved oxygen sag profile for the illustrated numerical example is presented, and the relationship between the total available aeration capacity and Lagrange multiplier is also developed treating weighting factors as parameters.     

城镇污水处理厂低浓度连续进水间歇曝气运行模式分析

根据南方城镇污水处理厂建成运行初期的实际运行情况,对低浓度进水的运行模式进行了分析和研究。运行中,污水处理厂MISS浓度调整为25g／L,采用曝气3h、停曝5h、连续进水的运行模式,实现了生物系统稳定运行,出水达标。     

A MODEL FOR PREDICTING LAKE SEDIMENT OXYGEN DEMAND FOLLOWING HYPOLIMNTETIC AERATION1

ABSTRACT: Hypolimnetic aeration is a widely used technique for lake restoration and fisheries enhancement. However, system design still depends on application of “safety factors” to observed oxygen demand rates, in large part because actual oxygen demand may be greater after aeration than before. Laboratory incubations of sediment show that sediment oxygen demand (SOD) rates follow mixed order kinetics, with an initial period of zero order reaction, followed by first order kinetics. The transition from zero to first order kinetics may correspond to the transition from laminar to turbulent flow. This suggests that SOD reaction kinetics are governed by thickness of the diffusive sublayer adjacent to the sediments. Therefore, zero and first order reaction regions correspond with oxygen diffusion limitation and substrate limitation, respectively. Such a mechanism would account for the induced oxygen demand observed following hypolimnetic aeration and would reconcile differences in SOD reaction orders noted in the literature. This paper describes development of equations based on laboratory SOD incubations for predicting induced oxygen demand following hypolimnetic aeration.     

微孔扩散管曝气试验

本文综术字在污水处理站使用离心鼓风机穿孔管大气泡浅 支暴气所引起的溶解氧不足。     

Intermittently aerated EMMC-Biobarrel (entrapped mixed microbial cell with Bio-barrel) process for concurrent organic and nitrogen removal

The PEMMC-Biobarrel (packed-bed of entrapped mixed microbial cells with Bio-barrel) process and MEMMC-Biobarrel (moving EMMC-Biobarrel) process were investigated for enhancing concurrent organic and nitrogen removal with applied intermittent aeration. For the PEMMC-Biobarrel process, the EMMC-Biobarrel carriers were employed at a packing ratio of 20%. In the MEMMC-Biobarrel process, the EMMC-Biobarrel carriers with a packing ratio of 10% were added along with the activated sludge (AS) in the bioreactor. Three different hydraulic retention times (HRTs) of 9, 6 and 4 h were applied. Aeration was provided intermittently at time schedules of 1 h air on/1 h air off, 1 h on/1.5 h off and 1 h on/2 h off. Nitrogen removal in the PEMMC-Biobarrel system was not improved by increasing the intermittent non-aeration time period. On the other hand, the MEMMC-Biobarrel process enhanced nitrogen removal with increasing non-aeration time even though the SCOD/N(TIN) ratio decreased from 6 to 4. Significant denitrification during the aeration cycle was observed in the MEMMC-Biobarrel process. The MEMMC-Biobarrel process demonstrated the most efficient organic and nitrogen removal at an HRT of 6 h with an intermittent aeration time schedule of 1 h on/2 h off. Nitrogen removal of 80% was achieved, which was about 15% higher compared to the AS system. TCOD and SCOD removal efficiencies were 80% and 75%, respectively.     

FIELD TESTING OF AN ICE-PRESERVING WINTER LAKE AERATION SYSTEM1

ABSTRACT: Artificial aeration is used to prevent winter fish kills due to oxygen depletion in ice-covered lakes. Conventional aeration by air bubble plumes and other techniques usually mixes the water column and produces hazardous open water in the ice cover. A non-mixing winter lake aeration system which creates a fish refuge was designed and field tested to oxygenate the water and maintain water temperature stratification in a lake such that no open water is created. The system uses a cascade aerator and has a design discharge and dissolved oxygen input rate of 85 1/s and 70 kg/d, respectively. Aerated water is discharged near mid-depth with minimum disturbance of the ambient water through a specially designed diffuser. The system was tested in a shallow 3 m deep lake of 17 ha surface area during two winters and was found to perform as expected. Significant photosynthetic production of dissolved oxygen under the ice-cover was also observed during snow-free periods.