厌氧氨氧化活性抑制、恢复与强化及工艺应用研究进展

厌氧氨氧化(Anaerobic ammonium oxidation,Anammox)工艺是一项节能高效的生物脱氮工艺,但实际应用中存在Anammox细菌增殖缓慢与活性受抑制的问题.首先介绍Anammox的基质与非基质,如亚硝酸、有机物以及无机物的抑制效应,在此基础上阐述调控运行参数以及流加菌种等活性恢复措施.重点评述外加无机碳、Anammox中间产物、Fe和导电材料等对Anammox的强化效果,并以代谢图形式系统总结3种Anammox代谢途径.最后着重探讨将Anammox作为主流工艺推广到处理实际废水时所面临的亚硝酸盐氧化菌(Nitrite-oxidizing bacteria,NOB)抑制和冬季水温低的问题,归纳使用游离氨和游离亚硝酸溶液淘洗NOB的方法以及选择合适反应器构型与培养方式等应对低温的对策;分析Anammox与反硝化间的协同作用以及将Anammox工艺拓展应用到烟气脱硝和芳香烃厌氧降解方面的潜力.提出未来需要在多因素联合抑制、Anammox生理特性和中间代谢机理以及抵御主流废水处理的不利因素等方面进行深入研究.     

厌氧氨氧化反应影响因素研究进展

厌氧氨氧化(Anammox)反应是指在厌氧或者缺氧条件下,厌氧氨氧化微生物以NO_2~--N为电子受体,氧化NH_4~+-N为氮气的生物过程。厌氧氨氧化反应是自养型生物脱氮反应,该过程无需外加有机碳源,在高氨氮低碳源废水处理方面具有重要应用价值。然而Anammox菌生长缓慢,最大生长率0.002 7 h~(-1),倍增时间长达10~12 d,对生长环境要求近乎苛刻,成为Anammox工艺工程化应用的最大瓶颈。因此,Anammox反应的影响因素一直是该领域的研究热点。文章系统总结了Anammox过程的主要影响因素,其中包括反应器类型、污泥性质、填料等反应器条件,温度、p H值、氧气、电磁场等环境因子,以及有机物、氮素、磷酸盐、盐度、金属离子等基质条件对Anammox启动和运行的最新研究进展,认为p H值接近中性、温度30~35℃、避光、严格厌氧等环境条件下,以反应器、填料和颗粒污泥相结合,降低污泥流失,并给予合适的基质和必要元素,可促进Anammox的快速增长。该文为Anammox工艺的基础研究和工程化应用提供了参考,并认为今后在各影响因素的联系、功能基因改性及极端环境驯化等方面仍需要加强研究。     

厌氧氨氧化污水处理工艺及其实际应用研究进展

厌氧氨氧化(Anammox)反应是指在厌氧或者缺氧条件下,厌氧氨氧化微生物以NO2--N为电子受体,氧化NH4+-N为氮气的生物过程。该过程是一种新型自养生物脱氮反应,反应无需外加有机碳源,且污泥产生量小,相对于传统硝化/反硝化脱氮工艺具有显著优势,对处理含高氨氮废水特别是低有机碳源废水具有重大的潜在实际应用价值。近年来,厌氧氨氧化为主体的污水处理工艺已经在各种类型废水处理中得到成功应用,取得了显著的经济和环境效益。综述了厌氧氨氧化反应中常用的亚硝化-厌氧氨氧化工艺(Sharon-Anammox工艺)和完全自养脱氮工艺(CANON工艺)的作用原理、环境调控因子与功能性微生物种群动态分布等最新研究进展,且阐述了两工艺在垃圾渗滤液、厌氧消化液和猪场养殖废水等低碳氮比废水的处理应用效能和最优化控制参数等,为厌氧氨氧化为主体的污水处理工艺的工程化应用提供了技术支撑。最后,总结并介绍了国内外厌氧氨氧化工艺现场规模化应用实例和控制参数,同时,对厌氧氨氧化污水处理工艺实际应用的研究前景及亟待解决的问题进行了展望,认为现场应用中Anammox菌的快速富集培养、有机碳源对Anammox菌的抑制效应以及厌氧氨氧化工艺的广谱适用性等将是厌氧氨氧化工艺大规模应用的难点和热点问题。为厌氧氨氧化工艺实际应用控制和推广提供了理论基础,具有重要的理论和现实意义。     

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.     

废水生物脱氮中N_2O和NO_x的产生和作用

废水生物脱氮中N2O和NOx来源于硝化、反硝化、厌氧氨氧化和化学反硝化等过程.电子受体和供体浓度、pH、缓冲剂类型、有机负荷、微生物种类及其相互作用等都会影响这些气态中间产物的产生.NO2能够氧化氨和强化好氧和厌氧氨氧化,NO能够阻止C2H2对好氧氨氧化活性的抑制,两者对好氧氨氧化活性的恢复至关重要.所有这些表明,废水生物脱氮的气态中间产物N2O和NOx在氮的生物转化中具有重要的正面作用,甚至必不可少.基于NO2曝气技术和Brocadiaanammoxidans与Nitrosomonas协同作用的废水生物脱氮新技术开发是今后一段时间的重要研究方向.图4参35     

影响厌氧氨氧化与甲烷化反硝化耦合的因素

氨氮、氮氧化物对产甲烷菌有一定的抑制作用,但可以通过驯化去除毒性.亚硝酸盐在厌氧氨氧化菌作用下与氨发生厌氧氨氧化反应.虽然厌氧氨氧化菌是自养菌,但具有异养代谢能力,并且NO2可提高厌氧氨氧化菌的活性.因此,通过特殊的反应器技术,将厌氧氨氧化菌与甲烷菌、反硝化菌复合在一个有利的微生态环境中,充分发挥它们之间的协同耦合作用,把有机物转化为清洁能源又同时脱氮,是极有前景的废水厌氧(缺氧)处理研究新方向.表1参31     

金属元素对厌氧氨氧化生化过程和工艺运行的影响

厌氧氨氧化为高效低耗生物脱氮技术,但金属元素对该工艺的作用存在两面性,一方面其促进作用可提高工艺处理效果,另一方面抑制作用使其工程应用受到一定限制.为此本文从生物化学和污水处理工艺的角度,系统地总结了国内外金属对厌氧氨氧化影响的研究现状,重点分析与讨论了不同金属元素对厌氧氨氧化细胞结构和相关酶蛋白活性等的影响和作用机理;综述了金属元素对厌氧氨氧化工艺运行的影响,讨论与分析了不同厌氧氨氧化工艺的半抑制浓度及活性修复方法.     

废水生物脱氮中N2O和NOx的产生和作用

废水生物脱氮中N2O和NOx来源于硝化、反硝化、厌氧氨氧化和化学反硝化等过程．电子受体和供体浓度、pH、缓冲剂类型、有机负荷、微生物种类及其相互作用等都会影响这些气态中间产物的产生．NO2能够氧化氨和强化好氧和厌氧氨氧化，NO能够阻止C2H2对好氧氨氧化活性的抑制，两者对好氧氨氧化活性的恢复至关重要．所有这些表明，废水生物脱氮的气态中问产物N2O和NOx在氮的生物转化中具有重要的正面作用，甚至必不可少．基于NO2曝气技术和Brocadia anammoxidans与Nitrosomonas协同作用的废水生物脱氮新技术开发是今后一段时间的重要研究方向．图4参35     

氨氮废水的厌氧氨氧化生物脱氮研究

利用从厌氧污泥中筛选和驯化的厌氧氨氧化（Anammox）菌直接启动UASB反应器,通过缩短水力停留时间（HRT）提高系统运行负荷,探讨水力停留时间对模拟废水脱氮性能的影响。结果表明,（1）富含Anammox菌的颗粒污泥能够快速启动反应器（只需14d）。（2）连续91d的HRT测试期间,系统具有良好的脱氮性能,且随着HRT的缩短,系统的脱氮效率具有波动上升的特点。NH4＋-N、NO2--N和TN（总氮）的平均去除率超过70.0%。（3）系统总氮容积负荷（TNLR）和总氮去除负荷（TNRR）最大值（以N计）分别为2.04kg·m-3·d-1和1.56kg·m-3·d-1。（4）系统能够比较好的遵循Anammox生物脱氮的理论途径：NH4＋-N、NO2--N的去除速率与NO3--N的生成速率的比例为1？1.15？0.22,与其相应理论值（1？1.32？0.26）非常接近。     

生物蛭石污水处理过程中氮的形态变化研究

为了探索天然蛭石作为湿地基质强化湿地脱氮效果的可行性,将天然蛭石填充有机玻璃,用废水培养挂膜获得生物蛭石,用以去除模拟污水中的氮。试验结果表明:生物蛭石柱对NH4 -N和T-N去除效果显著且稳定。生物蛭石滤柱中是以厌氧氨氧化作用为主的脱氮作用,溶解氧是影响厌氧氨氧化作用的重要因素。     

Recent advances in activity inhibition,recovery and enhancement,and application of the anaerobic ammonium oxidation process北大核心CSCD

Anaerobic ammonium oxidation (Anammox) is a biological process that has the advantages of saving energy and being highly efficient. However, there are some problems with it such as slow proliferation and activity inhibition of Anammox bacteria in practical applications. First, we introduce the inhibitory effects of Anammox by substrate and non-substrate materials, including nitrite, organic and inorganic substances, and others, and elaborated on activity recovery approaches such as controlling the operation parameters and adding sludge. The effects of the addition of inorganic carbon, Anammox intermediates, Fe, and conductive materials on Anammox are then reviewed in detail, and three Anammox metabolic pathways are summarized. Finally, we discuss the problems (including NOB inhibition and low temperature) and countermeasures when Anammox is applied for wastewater treatment as a mainstream technology, and we summarized the measures of NOB washout by free ammonia and free nitrite solutions and methods to cope with low temperatures, including selecting suitable reactor types and culture methods. Meanwhile, we analyzed the interactions among the intermediates and the synergy between Anammox and denitrification and suggest the potential of applying Anammox for flue gas denitrification and anaerobic aromatic hydrocarbon biodegradation. Further studies are suggested regarding multifactor composite inhibition, Anammox physiological characteristics, and intermediate metabolic mechanisms as well as regarding methods for avoiding adverse factors in mainstream wastewater treatment. © 2018 Science Press. All rights reserved.     

上海市典型污水处理厂污泥浸出液的化学和毒性评价

为了研究污水污泥在海洋环境中释放带来的生态风险,在分析上海7处典型污水处理厂污水污泥浸出液中重金属与溶解性有机碳的基础上,使用黑鲷,卤虫,三角褐指藻,纤细角毛藻和小球藻研究污水污泥浸出液对海洋生物的急性毒性作用和生长抑制作用。化学分析结果表明,所有样点的污水污泥浸出液中重金属总量均低于中国(GB5085.3-2007)与欧盟(EN12457.2-2002)关于危险废弃物的鉴别标准,但溶解性有机碳(DOC)含量超过欧盟标准1个数量级。毒性实验结果表明,黑鲷幼鱼对污水污泥浸出液的敏感性最强,其次是海洋微藻,卤虫无节幼体的敏感性较低;毒性综合分析结果表明,S2和S3点的污水污泥浸出液对海洋生物的综合生物毒性相对最高,而S4,S5的综合生物毒性最低,其中接纳污水为工业污水,且有机质与硫化物含量较低的污水污泥浸出液对海洋生物的综合生物毒性较低。     

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。     

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.     

Mechanistic insight into the biofilm formation and process performance of a passive aeration ditch (PAD) for decentralized wastewater treatment

• A Passive Aeration Ditch was developed to treat decentralized wastewater. • A model was developed to describe the process performance. • A high C/N ratio facilitates microbial growth but nitrification deteriorates. • A high salinity decreases both organic and nitrogen contaminants removal. Decentralized wastewater containing elevated salinity is an emerging threat to the local environment and sanitation in remote coastal communities. Regarding the cost and treatment efficiencies, we propose a passive aeration ditch (PAD) using non-woven polyester fabric as a feasible bubbleless aerator and biofilm carrier for wastewater treatment. Consideration has been first given to PAD’s efficacy in treating saline decentralized wastewater, and then to the impact of chemical oxygen demand-to-nitrogen (C/N) ratio and salinity on biofilm formation. A multispecies model incorporating the salinity effect has been developed to depict the system performance and predict the microbial community. Results showed that the PAD system had great capacity for pollutants removal. The biofilm thickness increased at a higher C/N ratio because of the boost of aerobic heterotrophs and denitrifying bacteria, which consequently improved the COD and total nitrogen removal. However, this led to the deterioration of ammonia removal. Moreover, while a higher salinity benefited the biofilm growth, the contaminant removal efficiencies decreased because the salinity inhibited the activity of aerobic heterotrophs and reduced the abundance of nitrifying bacteria inside the biofilm. Based on the model simulation, feed water with salinity below 2% and C/N ratio in a range of 1 to 3 forms a biofilm that can reach relatively high organic matter and ammonia removal. These findings not only show the feasibility of PAD in treatment of saline decentralized wastewater, but also offer a systematic strategy to predict and optimize the process performance.     

制药废水的可生物降解性与生物毒性研究

制药废水有机物含量高,难生物降解成分多,有些成分可抑制污泥活性或具有生物毒性.以某制药企业维生素生产的7个工段(W1 ～ W7)的排放废水为研究对象,用摇瓶试验评价了各工段废水的可生物降解性能,用瓦勃氏呼吸仪测试了各工段废水对污泥活性的抑制作用,用发光菌急性毒性试验评价了各工段废水经好氧生物处理前后的生物毒性变化.研究...     

微波碱解处理剩余污泥的厌氧消化性能

为了研究微波碱解预处理（microwave/NaOH pretreatment,MNP）剩余污泥在高温和中温条件下厌氧消化的性能,采用半连续完全混合式反应器分别研究了MNP处理后的剩余污泥在高温厌氧消化工艺（thermophilic anaerobic di-gestion process,TADP）和中温厌氧消化工艺...     

7种酚类化学物质对活性污泥的呼吸抑制作用

苯酚类化学物质是废水中常见的有机污染物,其对活性污泥的毒性数据对于污水处理厂稳定运行和化学品危害性评估具有重要意义。本研究采用活性污泥呼吸抑制试验(209)测定7种酚类化学物质对活性污泥的呼吸抑制作用。结果显示,2,6-二叔丁基苯酚和对特辛基苯酚对活性污泥未产生明显的毒性效应;2,4-二氯酚、2-苯基苯酚、4-硝基酚、4-氯酚和对甲酚等5种化学物质都对活性污泥呼吸有不同程度的抑制效应,3 h-EC50值分别为49.7、77.6、102、150.1和462 mg·L-1,构效关系分析结果表明-Cl、-NO2等官能团是导致活性污泥呼吸抑制效应增强的关键因素。在化学品生物降解性测试研究中,要确保有毒化学物质的测试浓度低于EC50值的1/10。     

A review on anammox process for the treatment of antibiotic-containing wastewater: Linking effects with corresponding mechanisms

• Anammox is promising for nitrogen removal from antibiotic-containing wastewater. • Most antibiotics could inhibit the anammox performance and activity. • Antibiotic pressure promoted the increase in antibiotic resistance genes (ARGs). • Antibiotic-resistance mechanisms of anammox bacteria are speculated. Antibiotic is widely present in the effluent from livestock husbandry and the pharmaceutical industry. Antibiotics in wastewater usually have high biological toxicity and even promote the occurrence and transmission of antibiotic resistant bacteria and antibiotic resistance genes. Moreover, most antibiotic-containing wastewater contains high concentration of ammonia nitrogen. Improper treatment will lead to high risk to the surrounding environment and even human health. The anaerobic ammonium oxidation (anammox) with great economic benefit and good treatment effect is a promising process to remove nitrogen from antibiotic-containing wastewater. However, antibiotic inhibition has been observed in anammox applications. Therefore, a comprehensive overview of the single and combined effects of various antibiotics on the anammox system is conducted in this review with a focus on nitrogen removal performance, sludge properties, microbial community, antibiotic resistance genes and anammox-involved functional genes. Additionally, the influencing mechanism of antibiotics on anammox consortia is summarized. Remaining problems and future research needs are also proposed based on the presented summary. This review provides a better understanding of the influences of antibiotics on anammox and offers a direction to remove nitrogen from antibiotic-containing wastewater by the anammox process.     

青岛城市污水厂污泥有机质、养分及重金属含量

对青岛市4个典型城市污水厂脱水污泥中有机质、养分及重金属指标进行了调查研究,结果表明,所调查的青岛市4个典型城市污水厂污泥中的有机质平均含量为48.58%,总氮、总磷、总钾平均含量分别为36 437.76 mg/kg、12 590.13 mg/kg2、791.55 mg/kg;青岛市4个典型城市污水厂脱水污泥中的重金属...