膜-生物反应器与普通活性污泥法处理啤酒废水试验

膜-生物反应器组合工艺由于用膜组件代替传统的二沉池而具有普通活性污泥法无法比拟的优点,研究对膜-生物反应器及普通活性污泥法的COD和NH₃ -N去除效率、降解动力学、微生物组成、活性污泥粒径分布等方面作了比较。      

广州市污水污泥堆肥在环境绿化中的应用

将广州市大坦沙污水处理厂产生的脱水生污泥与粉煤灰、稻草按质量比例4∶1.2∶1混合堆制而成的污泥堆肥,堆肥总养分含量高于农家肥中的鸡粪,无论单独施用或与化肥结合使用应用于草坪等园林绿地,均有明显效果。污泥堆肥在草坪土壤应用的肥效试验表明,污泥堆肥与化肥结合使用效果较好,能缩短草坪草出苗和成坪时间,显著提高建植初期草坪草的生物量,但每公顷施用纯污泥堆肥30t与60t比较两者草坪草生物量没有显著差异;污泥堆肥施用污染风险初步分析表明,土壤中的重金属含量、渗滤液中的NO3--N和全P含量随着污泥堆肥施用量的增加而明显提高,考虑到广东地处热带、亚热带,雨量丰富且暴雨多,土壤呈酸性的特点,在园林绿地等相对封闭的体系中施用本项目堆制的污泥堆肥,只要将年施用量控制在30t/hm2以下,是基本安全的。     

厌氧颗粒污泥对五氯苯酚脱氯过程中的影响因素

在间歇培养血清瓶中,研究了厌氧颗粒污泥对五氯酚脱氯过程中的影响因素.结果表明,葡萄糖、酵母膏和蛋白胨显著提高了PCP的脱氯速率.添加甲酸、乙酸、乙醇对PCP脱氯速率有一定提高,丙酸和丁酸对脱氯速率没有影响.20%氢气的加入对PCP脱氯速率的影响显著.废水中硝酸盐和硫酸盐等电子受体的存在降低了PCP的脱氯速率.微生物抑制剂氯仿、青霉素降低了PCP脱氯速率,表明厌氧微生物尤其是甲烷菌对还原脱氯有重要影响.PCP最佳还原脱氯温度为38℃,最佳pH为7,低的氧化还原电位(<-200mV)有利于脱氯的进行.图5参13     

污泥超声破解效应及厌氧消化性能研究

针对超声破解污泥的可行性进行了实验研究,重点考察了超声频率、比能耗、作用时间等因素对破解效应的影响,探讨了破解污泥的厌氧消化性能。结果表明,超声作用的施加可使污泥固体有效破解,污泥细胞内的活性有机物被释放至水相并形成溶解性有机物,表现为SCODCr的显著增加;采用低频、高比能耗及延长作用时间有利于获取高的SCODCr增加值;污泥在频率25kHz、比能耗2.0W/mL、作用时间30min条件下破解,其厌氧消化累计产气量可从破解前的268mL提高到473mL,相应TCODCr去除率、VS去除率分别从39.1%、33.5%提高至54.3%、61.7%。研究结果表明采用超声破解技术提高污泥的厌氧消化性是可行的。     

Mo6+对活性污泥系统反硝化性能的影响

采用对比实验的方法,在不同初始硝酸盐氮和COD质量浓度的条件下,对人工模拟的活性污泥系统投加不同质量浓度的Mo6 ,以此考察Mo6 对活性污泥系统反硝化性能的影响。结果发现,Mo6 的质量浓度小于5mg?L-1以下时能够促进硝酸盐氮的去除,质量浓度为1mg?L-1时促进效果最好。Mo6 的质量浓度在4mg?L-1以下时,可以使COD去除效率增加,质量浓度为2mg?L-1时有最佳促进作用。Mo6 的质量浓度小于1g?L-1时可提高反硝化活性污泥的TTC-脱氢酶活性,过高质量浓度则表现出抑制作用。综合Mo6 的对硝酸盐氮和COD去除的影响规律以及对活性污泥TTC-脱氢酶活性的影响,认为Mo6 在质量浓度为1mg?L-1时对反硝化的促进作用最强。     

污泥浓缩脱水及相关技术研究进展

文章对污泥浓缩、污泥调理、污泥脱水技术发展现状进行了介绍,着重对主流污泥脱水技术及设备选型进行了分析比较,强调了污泥处理技术具有各自的适用范围.此外还介绍了超声波技术在污泥处理领域应用的前景.     

Relationships between anaerobic consortia and removal efficiencies in an UASB reactor degrading 2,4 dichlorophenol (DCP)

To gain more insight into the interactions between anaerobic bacteria and reactor performances (chemical oxygen demand-COD, 2,4 dichlorophenol-2,4 DCP removals, volatile fatty acid-VFA, and methane gas productions) and how they depended on operational conditions the microbial variations in the anaerobic granular sludge from an upflow anaerobic sludge blanket (UASB) reactor treating 2,4 DCP was studied. The study was composed of two parts. In the first part, the numbers of methanogens and acedogens in the anaerobic granular sludge were counted at different COD removal efficiencies. The relationships between the numbers of methanogens, the methane gas production and VFA production were investigated. The COD removal efficiencies increased to 74% from 30% while the number of total acedogens decreased to 10 from 30 cfu ml(-1). The number of total methanogens and acedogens varied between 11 x 10(3) and 10 x 10(9)MPN g(-1) and 10 and 30 cfu ml(-1) as the 2,4 DCP removal efficiencies were obtained between 60% and 99%, respectively. It was seen that, as the number of total acedogens decreased, the COD removal efficiencies increased. However, the number of total methanogens increased as the COD removal efficiencies increased. Correlations between the bacterial number and with the removal efficiencies obtained in different operational conditions were investigated. From the results presented in this paper a high correlation between the number of bacteria, COD removals, methane gas percentage, 2,4 DCP removals and VFA was observed. In the second part, methanogen bacteria in the anaerobic granular sludge were identified. Microbial observations and biochemical tests were applied to identify the anaerobic microorganisms from the anaerobic granular sludge. In the reactor treating 2,4 DCP, Methanobacterium bryantii, Methanobacterium formicicum, Methanobrevibacter smithii, Methanococcus voltae, Methanosarcina mazei, Methanosarcina acetivorans, Methanogenium bourgense and Methanospirillum hungatei were identified.     

Immersion frying for the thermal drying of sewage sludge: an economic assessment

This paper presents an economic study of a novel thermal fry-drying technology which transforms sewage sludge and recycled cooking oil (RCO) into a solid fuel. The process is shown to have significant potential advantage in terms of capital costs (by factors of several times) and comparable operating costs. Three potential variants of the process have been simulated and costed in terms of both capital and operating requirements for a commercial scale of operation. The differences are in the energy recovery systems, which include a simple condensation of the evaporated water and two different heat pump configurations. Simple condensation provides the simplest process, but the energy efficiency gain of an open heat pump offset this, making it economically somewhat more attractive. In terms of operating costs, current sludge dryers are dominated by maintenance and energy requirements, while for fry-drying these are comparatively small. Fry-drying running costs are dominated by provision of makeup waste oil. Cost reduction could focus on cheaper waste oil, e.g. from grease trap waste.     

高负荷活性污泥法应用于中小城市污水处理的研究

针对目前二级城市污水处理厂工程投资高、运行费用高的特点,提出适合中小城市污水处理的工艺——高负荷活性污泥法（HAS）。该工艺不设初次沉淀池,负荷高,泥龄短,污泥沉降性能良好,不存在污泥膨胀,对有机物的去除以絮凝、吸附、沉淀作用为主,对COD、BOD,、SS都有较高的去除效果,对氮、磷有一定的去除作用,出水水质可满足《农田灌溉水质标准》的要求。     

城市污水污泥发酵制园林营养土中微生物的变化分析

通过桶装发酵装置,进行城市污水污泥发酵制园林营养土过程中微生物的变化研究,测试不同好氧-厌氧交替组的发酵温度以及细菌、真菌、放线菌数量等的变化,探讨发酵温度与微生物变化的规律.结果表明,夏季不同发酵方式的发酵温度在50℃以上的持续时间均长于冬季,且夏季好氧-厌氧交替发酵的发酵温度在55℃以上的持续时间长于好氧发酵;冬季与夏季的好氧、好氧-厌氧交替发酵后,堆料中的粪大肠菌群数量均达到了《城镇污水处理厂污泥处置园林绿化用泥质》(CJ 248-2007)的卫生学指标要求;夏季好氧-厌氧交替发酵过程中,厌氧后发酵温度有所下降,好氧后发酵温度又有所回升;无论好氧还是好氧～厌氧交替发酵中,细菌均为优势种群,真菌、放线菌数量比细菌数量低2～6个数量级.