污水处理中的污泥减量新技术

污水好氧处理会产生大量污泥，剩余污泥的处理成本高昂，减少污泥产量势在必行。文章介绍了代谢解偶联、增加维持能量消耗、隐性生长、微型动物捕食、高溶解氧工艺和膜生物反应器等污泥减量技术，比较了各种技术的优缺点，指出了不同技术结合将成为污泥减量技术的发展方向。     

污水厂污泥制轻质陶粒研究现状及应用前景

作为污水处理厂的副产物，污泥必须进行适当的处理。在介绍了国内外污水厂污泥制轻质陶粒的研究现状的基础上，从陶粒制备工艺、技术可行性、经济效益和环境效益等方面探讨了污水厂污泥制轻质陶粒的应用前景。     

好氧颗粒污泥工艺强化脱氮研究进展

好氧颗粒污泥是微生物通过自凝聚作用形成的一种特殊的生物聚集体,具有结构致密、沉降性能优异、抗冲击负荷能力强、多功能微生物分区定殖等特点,其在废水强化脱氮除磷与难降解有机物去除方面具有明显的技术优势.针对目前工业和养殖废水及城镇生活污水等碳氮比低、处理出水总氮达标压力大等突出问题,综述基于好氧颗粒污泥的全自养、同步硝化反硝化、短程硝化反硝化、短程硝化-厌氧氨氧化、异养硝化-好氧反硝化等强化脱氮工艺,介绍其脱氮机制及技术优势,阐明不同好氧颗粒污泥脱氮工艺的特点与颗粒污泥特性,同时总结各种工艺的启动条件及富集相应功能菌的好氧颗粒污泥的形成因素,评估不同工艺应用于实际废水生物处理的可行性.在此基础上进一步分析进水基质组成(不同碳氮比)、运行模式(连续曝气和间歇曝气)、运行条件(溶解氧浓度、温度和pH)等对好氧颗粒污泥工艺强化脱氮性能与稳定运行的影响.最后提出应进一步优化好氧颗粒污泥强化脱氮工艺的运行参数,解析好氧颗粒污泥微生物菌群功能,揭示好氧颗粒污泥形成与结构稳定的微生物学机理.     

投加硝化菌的活性污泥工艺硝化效率特性

研究了在活性污泥工艺中用投加硝化菌的方法提高硝化效率的特性，试验用富氮废水生成硝化污泥，并将其剩余硝化污泥投加于处理初沉市政污水的活性污泥工艺试验装置，研究结果表明，投加硝化菌能降低常规活性污泥工艺硝化的泥龄要求、改善硝化效果以及减少为低温稳定运行而增加的硝化反应器容积。     

长江三角洲地区城市污泥的综合生物毒性研究

运用发光细菌法对我国长江三角洲地区16个城市中54个污泥样品的综合急性生物毒性进行了测定,并以毒性较为稳定的HgCl2作为参比毒物,以发光细菌抑光率、相当标准毒物HgCl2质量浓度及百分数等级比较法毒性划分标准评价城市污泥的毒性。结果表明,供试的不需稀释测定毒性的城市污泥中,有13个是剧毒的,占样品总数30．95％;需稀释测定毒性的城市污泥中,毒性等级为Ⅰ级的8个,占样品总数66．67％。长江三角洲地区城市污泥大部分有较高的综合急性生物毒性,这与含多种高量的有毒重金属有关。城市污泥对发光细菌毒性的大小与城市污泥来源、污水处理工艺及污泥类型等因素有关。上海地区的污泥毒性大于江苏和浙江地区;42个毒性较小的污泥中,大部分氧化沟处理的城市污泥的毒性要大于A^2／O（厌氧-缺氧／好氧）处理的,12个毒性较大的污泥中处理工艺多为活性污泥处理与A^2／O处理;大部分以生活污水和混流污水为主的城市污泥毒性要高于以工业污水为主的城市污泥。     

好氧颗粒污泥特性、应用及形成机理研究进展

好氧颗粒污泥因具有良好的沉降性能、较高的生物量、对污染物较高的去除能力,以及在工程应用中占地面积较少和运行成本较低,近年来被广泛关注.本文综述了絮状污泥的颗粒化过程,好氧颗粒污泥形成的影响因素及其物理、化学和生物学特性.研究发现,好氧颗粒污泥在生活污水、高浓度有机废水和富含有毒有害物质的废水处理中均可发挥重要作用,可以高效去除污水中的氮磷污染物、工业废水中的有机物、毒性物质和重金属等.好氧颗粒污泥的形成机理存在4种假说,基于絮状污泥颗粒化过程中形成的胞外聚合物及其助凝作用被普遍认为是好氧颗粒污泥的形成机理.最后进行了问题分析和前景展望,认为突破培养过程相对漫长、培养条件相对严苛技术瓶颈的好氧颗粒污泥技术对废水处理效能的提升具有重要意义.图3参110     

城市污水厂污泥倾倒对海洋生物的毒性研究

以广州市和佛山市的5个城市污水处理厂的污泥为实验对象,选取费氏弧菌、蒙古裸腹溞、卤虫、裸项栉鰕虎鱼仔鱼4种不同营养级的海洋生物为受试对象,结合化学分析方法,研究广州区域周边污水污泥浸出液的生物毒性效应。结果显示各污水污泥浸出液的毒性均较大,且浸出液的Cu污染浓度较高;广州市污水污泥对4种受试生物的毒性效应要高于佛山市。从污泥毒性对受试生物的选择性方面分析,发现卤虫筛分能力强且灵敏度高,而费氏弧菌则相关性好且方法简捷。研究结果为反映城市污泥的生物毒性强度和选择合适毒性评价受试生物提供基础数据。     

污泥资源化利用系列泥质标准的编制问题

为解决污泥处置问题,防止二次污染,维护良好生态环境,提高资源化利用水平,促进循环经济的发展和生态型城市的建设,建设部提出完成污泥系列泥质标准的编制工作.文章结合广州市排水监测站的泥质标准研究工作,详细阐述了国内外污泥系列泥质标准的现状以及最新的泥质标准研究工作进展,重点对八个标准--<城镇污水处理厂污泥处置:分类>、<城镇污水处理厂污泥处置:混合填埋泥质>、<城镇污水处理厂污泥泥质>、<城镇污水处理厂污泥处置:园林绿化用泥质>、<城镇污水处理厂污泥处置:农用>、<城镇污水处理厂污泥处置:焚烧用泥质>、<城镇污水处理厂污泥处置:土地改良用泥质>和<城镇污水处理厂污泥处置:制砖用泥质>中的控制项目、部分限值以及项目特点进行了研究和讨论,并对今后的研究方向进行了展望.     

好氧颗粒污泥实现同步硝化反硝化

采用人工配制的模拟生活污水，通过对运行条件的调控，在序批式反应器(SBR)中培养出了高活性的好氧颗粒污泥，颗粒污泥浓度达到4．55g/L以上，SVI值在32.5左右，反应器对于COD、NH3—N的去除率分别在83.6％—92.8％和82.3％—98.5％之间。实验结果表明：由于好氧颗粒污泥的存在，SBR反应器内发生了同步硝化反硝化(SND)反应，而不是通常所认为的顺序式硝化反硝化(SQND)反应。     

城市污水处理厂污泥处理处置的政策分析

简要介绍了城市污水处理厂污泥处理处置技术，提出污泥产业发展政策的建议，指出土地利用是符合我国国情的污泥处置的方向之一：污泥处理技术主要有减量化、浓缩、脱水、消化、堆肥等；污泥处置技术主要有焚烧、填埋、土地利用、建材利用等。污泥处理处置应按照减量化、稳定化、无害化原则，鼓励污泥资源化综合利用。合理确定污水处理厂污泥处理处置设施的布局和设计规模；鼓励对污泥处理处置给与税、费优惠政策，明确将污泥处理处置的运营费用列入污水排污收费范围，建立科学的价格补偿机制；政府在污泥产业发展中起着较为重要的作用，主要体现为服务与监督，包括承诺、保障和协调三个方面。     

制革废水处理系统各级出水的生态毒性评价

采用生态毒理学常用的大型溞（Daphnia magna）和活性污泥（activated sludge）作为试验系统,对制革废水处理系统各个环节出水进行毒性试验,以评价其处理效果。按照OECD标准试验方法,选取本实验室繁殖的大型溞（溞龄小于24 h）,和采自以处理生活污水为主的污水处理厂活性污泥,分别使用重铬酸钾和3,5-二氯酚作为参比物验证大型溞和活性污泥的毒性敏感性。以大型溞活动抑制和活性污泥呼吸抑制作为毒性终点,利用48 h静态试验和3 h曝气试验分别评价水样对于大型溞活动和活性污泥呼吸作用的急性毒性效应。统计各试验组大型溞的活动情况和活性污泥的呼吸速率,分别将其与空白对照组进行比较,计算大型溞的活动抑制率和活性污泥的呼吸抑制率,采用Bliss法统计制革废水处理系统各个环节出水对大型溞和活性污泥的半数抑制浓度（EC50）。结果表明：制革废水依次经过厌氧脱硫反应器、脱色厌氧反应器、微曝气反应器和厌氧氨氧化反应器的生物处理系统处理,其出水对大型溞和活性污泥的急性毒性已大为降低。进水、厌氧脱硫反应器出水、脱色厌氧反应器出水、微曝气反应器出水和厌氧氨氧化反应器出水对大型溞活动抑制试验的48 h-EC50分别为41.3%、32.2%、48.0%、91.2%和无抑制作用;活性污泥呼吸抑制试验3 h-EC50则分别为178.2%、101.5%、689.7%、184.6%和无抑制作用。总体上毒性呈现逐渐降低的趋势,而且大型溞比活性污泥更为灵敏。大型溞和活性污泥的生态毒性结果与化学分析的结果相互补充,可为制革废水处理提供预警和效果评价提供科学依据。     

活性污泥吸附预处理重油裂化制气废水

利用剩余活性污泥对含有高浓度芳香族化合物的重油裂化制气废水进行预处理的研究并提出了合适的吸附条件。结果表明，活性污泥吸附预处理对COD和悬浮物有明显的去除效果，而且可以提高废水BOD5／COD的比值，另外还有降解芳香族化合物的作用，使进入生物处理系统的废水的可生物降解性有明显的改善。这一方法为利用普通废水生物处理系统中产生的剩余活性污泥来预处理难降解的工业废水提供了一条有效的途径。     

Verhalten von Nanosilber in Kläranlagen und dessen Einfluss auf die Nitrifikationsleistung in Belebtschlamm

Background, aim and scope The application of nanosilver is increasing. Knowledge on the fate and behavior of nanosilver in wastewater and wastewater treatment plants is scarce. Studies under real world conditions are completely lacking. We studied (1) the impact of nanosilver on the nitrification of sewage sludge, (2) quantified the mass flow of nanosilver in a pilot-plant, and (3) verified the mass balance in a full-scale municipal wastewater treatment plant where nanosilver is introduced to the municipal plant by an indirect discharger. Materials and Methods The addition of four different nanosilver additives on ammonia oxidation in activated sludge has been studied in batch-reactors at two concentrations (1, 100?mg/L Ag) with two exposure times (2?h, 6?days). The pilot-plant treating 70 population equivalents of domestic wastewater is operated with a 12?day sludge age. Nanosilver was applied to the activated sludge tank within two sludge ages. The silver concentrations were measured in sludge and effluent samples during dosing and the following two sludge ages. The adsorption and speciation of silver particles has been analyzed using scanning electron microscopy (SEM) coupled with energy dispersive X-ray spectroscopy (EDX). Influent, effluent and sludge were sampled on a full-scale plant (60?000 equivalent inhabitants) and analyzed for silver. Results Silver nitrate, metallic nanosilver, nano-scaled silver chloride and microcomposite silver did not show any effect on ammonia oxidation after the addition of 1?mg/L Ag to the activated sludge (corresponding to 250?mg Ag per kg solids). In contrast, 100?mg/L Ag inhibited the nitrification process by 100?% after the addition of silver nitrate and 20–30?% after addition of colloidal polymer-coated nanosilver. A complete mass balance of the pilot-plant, a steady-state system with known fluxes, demonstrates significant enrichment of silver in the sewage sludge (96?%) after the addition of silver chloride to the plant and small losses of silver into the secondary effluent (4?%). The mass fluxes are similar to metallic colloidal nanosilver investigated under the same conditions. The mass balance has been consistently confirmed by the full-scale study in a municipal wastewater treatment plant. The silver fluxes correspond to the fluxes of the suspended solids in sludge and effluent. Overall, it is estimated that from public wastewater treatment plants about 4–40?mg/a Ag per inhabitant equivalent are discharged annually to the receiving water. The analysis by SEM-EDX demonstrates adsorption and incorporation of nanosilver on biological flocs. This method yields first insight into complex building and transformation of silver associated with sulfide after adding metallic nanosilver and silver chloride to wastewater. Discussion Silver ions released from nanosilver react immediately with large amounts of chloride present in wastewater to form silver chloride. Silver ions may react with organic ligands or sulfide groups additionally. Consequently, even silver nitrate added with 1?mg/L Ag (250?mg Ag/kg TS) to activated sludge did not inhibit nitrification activity. Very high amounts of nanosilver, i.?e. 100?mg/L Ag, overburdened the system and equilibrium condition between silver ion release and ligands was not reached. The mass balance reflects the excellent attachment of nanosilver to activated sludge and biological flocs. Therefore, the main elimination process of nanosilver is attachment to the activated sludge. The elimination of nanosilver is high compared to organic and inorganic micro pollutants omnipresent in wastewater. Any further reduction of suspended solids in the effluent water will reduce the silver load. Conclusions Generally, in wastewater nanosilver occurs bonded to activated sludge flocs and therefore the elimination of nanosilver is efficient under operation conditions typical for wastewater treatment plants. The major fraction of nanosilver is removed from the system by the excess sludge withdrawal. Nonetheless, the efficiency may be further improved by a tertiary filtration step. All analyses of influent, effluent and sludge confirmed that silver exists as silver sulfide. Due to a negligible water solubility of this silver species, silver ions are not subsequently released. Recommendations and perspectives Nanosilver research should be driven to the identification of transformation processes in real environmental matrices and the influence of coatings on the adsorption behavior. There is no need for action to take special measures for nanosilver removal in the area of municipal wastewater treatment plants compared to ubiquitous hazardous organic pollutants may present in wastewater. Nevertheless, source control measures following the precautionary principle should be performed.     

沸石生物联合吸附再生工艺及铵沸石再生

简述了沸石生物联合吸附再生的工艺原理,重点讨论吸附了NH 4的沸石粉的生物再生.结果表明,沸石和液相之间的NH 4是一种动态的离子交换平衡,污水的电导率对吸附了NH 4的沸石粉的NH 4解吸量有明显的影响;污水中阳离子对吸附了NH 4的沸石粉的再生率可达40%-50%,在微生物的硝化作用下可达94%.沸石生物联合吸附再生工艺中,吸附了NH 4的沸石粉的再生是"化学再生"和"生物再生"相结合的过程,生物硝化作用促进了沸石相中NH 4的解吸.     

干扰素生产废水处理试验及生物相分析

采用水解酸化与生物接触氧化组合工艺对干扰素生产废水进行试验研究,并考察其处理效果,观察生物接触氧化工艺中生物相。结果表明：该组合工艺对出水COD的去除率大于90%,出水COD低于40 mg/L,且运行稳定后生物接触氧化槽中污泥浓度较低。对生物相的显微镜观察可知生物接触氧化槽中生物相种类以藻类为主。     

二级SBR法处理高浓度氨氮化工废水研究

用直接活性污泥法完成了各反应器的污泥驯化启动。二级ＳＢＲ工艺主要由硝化ＳＢＲ和反硝化ＳＢＲ反应器构成,其中硝化ＳＢＲ反应器采用悬浮生长法和固定生物膜法两种工艺作对比试验。结果表明,后者较前者具有更大的ＮＨ３－Ｎ容积负荷,最大可达７６６．５４ｍｇＬ＾－１ｄ＾－１;而且能节省碱的消耗量１１．０％～３８．７％和反硝化所需碳源量为３０％～４０％。在ｔＨＲ为２４ｈ的条件下,二级ＳＢＲ法能处理ρＩｎ（ＮＨ３－     

啤酒废水处理工程设计

桂林漓泉有限公司污水处理厂经过改造,采用UASB－SBR工艺进行啤酒废水处理。处理后出水水质指标：COD＝35．7mg／L,BOD＝10mg/L,达到GB89790－1996《国家污水综合排放标准》的一级标准。改造后的工具具有投资少,占地面积小,结构紧凑,高效低耗,出水水质好,剩余污泥少,可回收能源等优点。     

驯化菌株降解油制气废水能力的比较

从3种污泥中驯化筛选出10种菌株,研究了各菌株对油制气废水不同污染指标的处理能力差别,以及各菌株对废水中芳烃化合物的降解能力.结果表明,各菌株可在初始阶段提高废水的BOD值,在高低废水浓度条件的降解能力基本一致;酚的去除率可达93.9%,但对废水中氨氮的去除率小于27.3%;实验采用的3种菌株对废水中的芳烃化合物都能降解,但其对芳环数≤3的芳烃化合物的降解能力强于对芳环数为4~6的芳烃化合物的降解能力.图4表2参10     

Mechanism on minimization of excess sludge in oxic-settling-anaerobic (OSA) process

The oxic-settling-anaerobic (OSA) process is a promising wastewater treatment technique for efficiently reducing sludge production and improving the stability of process operation. In this paper, the possible factors of sludge reduction such as sludge decay, uncoupled metabolism, and anaerobic oxidation with low sludge production were discussed in the OSA process. It has been confirmed that sludge decay is the decisive cause in the OSA process, accounting for 66.7% of sludge production reduction. Sludge decay includes hydrolysis and acidogenesis of dead microorganisms and particle organic carbon adsorbed in sludge floc and endogenous metabolism. By batch experiments, it has been proven that there is energetic uncoupling in the OSA system since microorganisms were exposed to alternative anaerobic and aerobic environment. It accounts for about 7.5% of sludge production reduction. Soluble chemical oxygen demand (SCOD) released from the anaerobic sludge tank in the OSA process was used as the substrate for cryptic growth. The substrate was used for anoxic denitrifying, anaerobic phosphorus release, sulfate reduction, and methane production. These anaerobic reactions in the sludge anaerobic tank have lower sludge production than in the aerobic oxidation when equivalent SCOD is consumed, which may lead to approximately 23% of sludge reduction in the OSA process. It has been concluded that multiple causes resulted in the minimization of excess sludge in the OSA system. The microbial community structure and diversity of sludge samples from the CAS (conventional activated sludge) and OSA systems were investigated by 16 SrDNA PCR-DG-DGGE (polymerase chain reaction-double gradient-denaturing gradient gel electrophoresis). DGGE profile and cluster analysis showed more abundant species in the OSA system contrasting to microbial communities in the CAS system.