法国某生活污水厂污泥好氧消化工艺运行研究

为了提高出水质量，法国小镇Cagnes—sur—Mer的生活污水处理厂从2008年初开始实施高有机负荷的运行，但同时这也提高了出泥产量。由于污泥的处理费用及搬运污泥的交通费用很高，水厂对污泥进行了污泥好氧稳定工艺，工艺使用纯氧机（VSA装置）就地利用空气制氧。工艺投入运行后，每日对好氧消化池的入泥和出泥进行采样和检测（MLSS、MLVSS、pH、COD、DRYNESS etc）以建立完整的运行数据。污泥经好氧消化作用后其有机物含量减少60％以上，每月减少40吨的出泥。同时，消化池的使用还使水厂周日也能对曝气池中的污泥进行抽取，缓解了以往由于周日停止排泥而导致周一曝气池中污泥浓度过大的问题。从而达到优化出水水质的目的。消化池中的温度维持在40℃左右，因为反应为放热反应，所以无需加热设备。此项目所收集到的数据将为这种工艺的发展提供帮助。同时也可以为那些想要减少出泥量的水厂提供一种新的方法。因为它投资小，见效快，操作简单。     

好氧颗粒污泥中胞外聚合物的提取、组成及空间分布研究进展

好氧颗粒污泥具有比传统活性污泥更加优越的性能，然而好氧颗粒污泥的稳定性限制了该技术的工业应用和推广。积累在颗粒表面的胞外聚合物（EPS）和好氧颗粒污泥系统长期运行的稳定性能有关。本文回顾了好氧颗粒污泥中EPS的成分、提取方法、在颗粒中的空间分布及EPS在颗粒化进程和稳定状态的作用，探讨了好氧颗粒污泥中EPS研究现状和不足，对亟待研究的内容提出了建议，以便为国内好氧颗粒污泥深入研究和工业应用提供参考。     

城市污水厂混合污泥好氧消化处理研究

以城市污水处理厂的初沉污泥与剩余污泥的混合污泥为对象,研究了影响污泥好氧消化处理的各项因素.通过测定氧摄取速率(OUR)和此污泥好氧速率(SOUR),对实验结果进行了探讨.     

解偶联技术在污泥减量化过程中的影响研究

针对污泥处理处置过程中的环境问题和经济问题,将传统的活性污泥工艺(CAS)与好氧—沉淀—厌氧工艺(OSA)对比,研究了两种工艺对污泥减量化的影响,分析了两种工艺对废水中COD浓度、COD去除效率、氨氮浓度及SVI值的影响,并指出OSA工艺运行稳定,抗冲击能力强,其引起的解偶联代谢能促进污泥产率下降。     

A2/O工艺处理焦化废水工程实例

本文介绍了采用厌氧-缺氧-好氧生物脱氮工艺（简称A^2／O工艺）处理焦化废水的工程设计和运行基本情况，并进行了分析总结。     

溶解氧对好氧颗粒污泥影响的研究进展

好氧颗粒污泥技术是一种新颖废水处理技术。溶解氧(DO)是好氧颗粒污泥形成和稳定运行的一个重要参数。好氧颗粒污泥需要的曝气量大,能耗高。高曝气量带来的高DO浓度不利于氨氮通过SND去除。当DO扩散在颗粒内部受到限制时,颗粒中心形成的厌氧层不利于颗粒污泥的长期稳定运行。本文系统分析了DO浓度对好氧颗粒污泥影响的国内外研究现状,对好氧颗粒污泥中DO浓度这一重要参数的研究进行了总结。研究在低DO浓度下保持好氧颗粒污泥的稳定性有利于降低运行成本,采取合适的方法降低颗粒内部的扩散限制有利于增强颗粒的稳定性能。     

粪渣污泥上清液和填埋场渗滤液混合处理工程分析

针对深圳市的情况,提出将粪渣污泥脱水上清液和玉龙坑垃圾填埋场渗滤液进行混合处理的工程方案。经过比较,推荐上清液和渗滤液混合废水的处理采用ＵＡＳＢ和好氧生物处理工艺,脱水粪渣和剩余污泥的处理则采用高温好氧堆肥的方案,使排放出水达到排放标准的要求下,做到了污泥的资源化利用,工程和运行管理方面也是可行的。     

水解(酸化)-好氧工艺处理混合工业废水试验研究

水解（酸化）＋好氧工艺可以有效地用于城市污水与工业废水处理，试验研究了不同工况条件下，水解（酸化）＋好氧工艺处理混合工业废水的效果，通过投加悬浮填料对水工艺过程进行优化，使其处理系统更为有效。在总的水力停留时间分别为11.5h、14.5h、19.0h,CODCr总的平均除率分别为72.1%、76.7%、77.6%,BOD5的去除率为89.6%、90.7%、91.5%，废水经水解（酸化）处理后，BOD5／CODCr有上升趋势，水解时间3.5h、4.5h、6h对应的BOD5／CODCr比值分别提高了3％、11％、17％，表明水解（酸化）提高了混合工业废水的可生化性。针对上海市某工业区混合废水建议水解（酸化）时间控制在6h以上、好氧反应控制在10.0h。     

复合好氧+BAF处理技术

由沈阳光大环保科技有限公司开发的复合好氧+BAF处理技术,主要应用于食品、屠宰等行业的污水处理。主要技术内容(1)复合好氧技术:采用生物选择、悬浮和固定生化微生物处理系统为一体,较好地解决了运行中污泥膨胀问题,能够高效稳定地去除溶解性有机物质,是传统好氧处理技术的综合与提高,该工艺污泥龄长、产泥     

好氧颗粒污泥同时脱氮除磷技术研究

采用序批式活性污泥法(SBR)处理新疆油田公司准东石油基地污水,作为生物膜的一种特殊形式,介绍了该工艺的优点,在适宜的运行条件下进行实验。讨论了好氧颗粒污泥脱氮以及除磷的过程,分析了该工艺对氮、磷的去除率及好氧颗粒污泥在好氧、缺氧条件下的吸磷情况,当进水氨氮、磷和乙酸碳浓度分别为38.2 mg/L、27.7 mg/L和134.6 mg/L,MLSS和MLVSS分别为7.0 mg/L、6.4 mg/L时,氨氮、总无机氮、磷、乙酸碳的平均去除率分别达到98.8%、90.2%、98.9%、97.2%.     

Land application of phosphorus-laden sludge: a feasibility analysis

An investigation was conducted to examine aerobic digestion of the phosphorus-laden sludge produced at the Regina Wastewater Treatment Plant and feasibility of land use of this sludge combined with the dewatered anaerobically digested primary sludge from this plant. Experimental studies showed that aerobic digestion can be employed for the stabilization of the chemical sludge. Results of the feasibility analysis showed that mixing the two digested sludges met the heavy metal criteria set by various guidelines for agricultural use, presented the advantage of an increased concentration of nutrients and a decreased concentration of heavy metals, and a longer useful life of the agricultural site compared to using dewatered anaerobically digested primary sludge alone. Land application of the mixed digested sludges would be a more appropriate method of sludge disposal compared to the present practice of landfilling the dewatered sludge and lagooning the chemical sludge.     

Performance of sequential anaerobic/aerobic digestion applied to municipal sewage sludge

A promising alternative to conventional single phase processing, the use of sequential anaerobic-aerobic digestion, was extensively investigated on municipal sewage sludge from a full scale wastewater treatment plant. The objective of the work was to evaluate sequential digestion performance by testing the characteristics of the digested sludge in terms of volatile solids (VS), Chemical Oxygen Demand (COD) and nitrogen reduction, biogas production, dewaterability and the content of proteins and polysaccharides. VS removal efficiencies of 32% in the anaerobic phase and 17% in the aerobic one were obtained, and similar COD removal efficiencies (29% anaerobic and 21% aerobic) were also observed. The aerobic stage was also efficient in nitrogen removal providing a decrease of the nitrogen content in the supernatant attributable to nitrification and simultaneous denitrification. Moreover, in the aerobic phase an additional marked removal of proteins and polysaccharides produced in the anaerobic phase was achieved. The sludge dewaterability was evaluated by determining the Optimal Polymer Dose (OPD) and the Capillary Suction Time (CST) and a significant positive effect due to the aerobic stage was observed. Biogas production was close to the upper limit of the range of values reported in the literature in spite of the low anaerobic sludge retention time of 15 days. From a preliminary analysis it was found that the energy demand of the aerobic phase was significantly lower than the recovered energy in the anaerobic phase and the associated additional cost was negligible in comparison to the saving derived from the reduced amount of sludge to be disposed.     

原子荧光法测定污泥中总汞的不确定度评定

对王水消解-原子荧光法测定污泥中总汞的不确定度进行评定,从测定过程和计算方法的角度,对样品称量、曲线拟合、样品消解、稀释、仪器测量重复性及污泥含水率等影响不确定度的分量进行分析。结果表明：影响原子荧光法测定污泥中总汞的不确定度的主要因素是工作曲线的非线性和样品消解过程造成的损失,其次是样品消解液的稀释和仪器重复测定,而样品称量与污泥含水率的影响较小,可忽略不计。     

市政污泥与高浓度废弃物的厌氧共消化：一种生物质能源净产生的途径

厌氧共消化是一种绿色、实用的回收废弃物中能源的技术。本文介绍了厌氧共消化技术的原理，并介绍了美国佐治亚州F. Wayne Hil水资源处理中心采用油脂废弃物（FOG）和含糖工业废水与市政污泥进行连续流厌氧共消化的实际应用案例。结果表明，厌氧共消化可显著提高甲烷产量达2倍以上，甲烷产量随着高浓度有机废弃物负荷率及厌氧消化反应器停留时间的延长而增加，且COD和VS降解率可保持在合理范围内，经济效益显著。     

现代分子生物学技术在活性污泥微生物菌群多样性研究中的应用

以活性污泥技术为主体的好氧工艺是污水生物处理技术方面应用较为广泛的方法。随着现代分子生物学技术的不断发展,人们对活性污泥中微生物菌群多样性的认识逐渐深化,大量用传统方法未检测到,但在活性污泥中发挥关键作用的微生物逐渐引起研究学者的重视。现代分子生物学技术以FISH技术、实时荧光定量PCR技术、DGGE／TGGE技术、16SrRNA序列比较、T—RFLP技术、AFLP技术等为代表已成为研究微生物微观形态及种群结构特征的主要手段。文章就这些技术在活性污泥微生物菌群多样性研究中的应用进行了总结,为进一步研究污水处理领域活性污泥的微生物菌群多样性提供了必要的依据。     

Modeling of real scale waste activated sludge anaerobic digestion process by Anaerobic Digestion Model 1 (ADM1)

In this study, real-scale wastewater treatment plant (Hurma WWTP) sludge anaerobic digestion process was modeled by Anaerobic Digestion Model (ADM1) with the purpose of generating the data to understand the process better by contributing to the prediction of the process operational conditions and process performance, which will be a base for future anaerobic sludge stabilization process investments.

Real-scale anaerobic sludge digestion process data was evaluated in terms of known process and state variables and also process yields. Average VS removal yield, methane production yield, and methane production rate values of the anaerobic sludge digestion unit were calculated as 46.4%, 0.49 m³CH₄/kg VS_removed, and 0.33 m³ CH₄/m³day, respectively. In this study, ADM1 was intended to predict the behavior of real-scale anaerobic digester processing sewage sludge under dynamic conditions. To estimate the variables of real-scale sludge anaerobic digestion process with high accuracy and to provide high model prediction performance, values of the four parameters (disintegration rate constant, carbohydrate hydrolysis rate constant, protein hydrolysis rate constant, and lipid hydrolysis rate constant) that have strong effects on structured ADM1 were estimated by using the parameter estimation module in Aquasim program and their values were found as 0.101, 10, 10, and 9.99, respectively. When the numbers of kinetic parameters with the processes included in ADM1 along with the dynamic and non-linear structure of the real scale anaerobic digestion were taken into consideration, model simulations were in good agreement with measured results of the biogas flow rate, methane flow rate, pH, total alkalinity, and volatile fatty acids.