限氧自养硝化-反硝化生物脱氮新技术

限氧自养硝化—反硝化是部分硝化与厌氧氨氧化相耦联的生物脱氮反应过程,通过严格控制溶解氧在0．1～0．3mg·L^-1,实现硝化反应控制在亚硝酸阶段,然后以硝化阶段剩余的NH4^+作为电子供体,在厌氧条件下实现反硝化,该反应过程是完全的自养硝化—反硝化过程,具有能耗低、脱氮效率高、反应系统占地面积小等优点,适用于处理COD／NH4^+—N低的废水,是一种非常有应用前景的生物脱氮技术,文中详细介绍了限氧自养硝化—反硝化生物脱氮反应过程的研究进展,讨论了其微生物学机理及应用前景。     

厌氧氨氧化菌特性及其在生物脱氮中的应用

在无分子氧环境中,同时存在NH4^＋和NO2^-时,NH4^＋作为反硝化的无机电子供体,NO2^-作为电子受体,生成氮气,这一过程称为厌氧氨氧化。目前已经发现了3种厌氧氨氧化菌（Brocadia anammoxidans,Kuenenia stuttgartiensis,Scalindua sorokinii）;对厌氧氨氧化菌的细胞色素、营养物质、抑制物、结构特征和生化反应机理的研究表明,厌氧氨氧化菌具有多种代谢能力。基于部分硝化至亚硝酸盐,然后与氨一起厌氧氨氧化,以及厌氧氨氧化菌与好氧氨氧化菌或甲烷菌的协同耦合作用,提出了几种生物脱氮的新工艺（ANAMMOX、SHARON—ANAMMOX、CANON和甲烷化与厌氧氨氧化耦合工艺）。     

基于氨单加氧酶基因的自养脱氮菌群结构分析

全程自养脱氮是一种在高氨氮低溶氧条件下完全由自养菌群作用脱除氮素的现象.以全程自养脱氮污泥为研究对象,特异性扩增氨单加氧酶活性基因amoA片段,建立克隆文库并对克隆序列进行系统发育学分析,考察全程自养脱氮系统从建立到退化过程中氨氧化菌的结构变迁.结果表明:Nitrosomonas oligotropha和Nitrosomonas europaea细菌是系统中的主要氨氧化菌,而随着系统的退化前者逐渐被后者完全取代,而氨氧化菌的种群变迁可能并不是全混流系统全程自养脱氮效率下降的原因.     

生物电化学耦合厌氧氨氧化强化脱氮及其微生物群落特征

为探究生物电化学强化厌氧氨氧化(anaerobic ammonia oxidation,anammox)脱氮作用过程,采用双室微生物电解池(microbial electrolysis cell,MEC)富集电活性微生物,构建耦合厌氧氨氧化阴极的生物电化学系统。具体地,在外加0.2 V电压条件下改变不同总氮进水浓度于30°C进行暗培养批次实验研究,结合循环伏安法、电化学阻抗谱、高通量测序方法等多种表征手段研究了强化脱氮机理。结果表明,在初始总氮浓度分别为200、300和400 mg/L时对应获得了96.9%±0.3%、97.3%±0.4%和99.0%±0.3%的总氮去除率,且阴极电极生物膜表现出良好的电化学活性。高通量测序结果表明外加电压富集了除厌氧氨氧化菌以外的其他脱氮功能菌群:反硝化菌(Denitratisoma)、Limnobacter和氨氧化菌SM1A02和Anaerolineaceae、亚硝化菌(Nitrosomonas europaea)和硝化螺菌属(Nitrospira)等,这些具有电化学活性的微生物构成了体系的氨氧化胞外产电菌(ammonium oxidizing exoelectrogens,AOE)和反硝化电养菌(denitrifying electrotrophs,DNE),它们连同厌氧氨氧化菌Candidatus Brocadia构成了系统的脱氮微生物群落结构。AOE和DNE的种间直接电子传递作用协同厌氧氨氧化是强化系统总氮去除的关键原因。     

溶解氧对单级自养脱氮系统功能菌数量的影响

摘要：【目的】研究溶解氧（Dissolved oxygen, DO）对单级自养脱氮系统功能菌数量的影响,为系统运行操控提出理论指导。【方法】从不同DO水平下的单级自养脱氮反应器中,分别提取活性污泥及生物膜样品基因组DNA,通过特异引物扩增系统内亚硝化菌（Ammonia oxidizing bacteria, AOB）、硝化菌（Nitrite oxidizing bacteria, NOB）及厌氧氨氧化菌（Anaerobic ammonia oxidizing bacteria, ANAMMOX）基因序列,PCR产物经回收克隆测序后,证实扩增产物为AOB、NOB及ANAMMOX 16S rDNA 保守序列,以含该序列的重组质粒作为定量PCR标准品。用荧光定量PCR技术对单级自养脱氮系统中各类功能菌进行定量分析。【结果】高DO有利于亚硝化菌AOB及硝化菌NOB生存,同时,活性污泥中AOB、NOB数量多于生物膜。DO对厌氧氨氧化菌ANAMMOX数量影响明显,高DO浓度将对ANAMMOX数量产生直接抑制,低DO浓度水平时,由于系统内缺乏厌氧氨氧化反应的电子受体NO3-或NO2-,也将间接影响ANAMMOX数量。【结论】本试验研究条件下,DO为(曝气)2.0/(停曝) 0.4 mg/L时系统运行效能最佳,ANAMMOX数量最多,AOB、NOB及ANAMMOX在此时构成一个协同代谢的稳定状态。     

盐分对生物脱氮工艺中硝化反应的影响与机理

高盐废水来源广泛,在利用生物脱氮法处理高盐含氮废水时,盐分会对生物脱氮产生抑制作用.硝化反应是生物脱氮工艺中的关键过程,研究盐分对硝化反应的影响机理具有重要意义.本文概述了盐分对废水生物脱氮过程中硝化反应影响的研究进展,总结了盐胁迫对好氧氨氧化过程、亚硝酸盐氧化过程中硝化效率和反应特性的影响规律,并分析了盐分对硝化微生物细胞形态、生物絮体结构和胞外聚合物特性变化以及菌群结构的影响,系统阐述了盐胁迫下的硝化反应机理,为高盐分高铵氮废水生物脱氮工艺设计提供理论指导.
     

异养硝化复合菌强化处理含氮废水脱氮性能研究

针对传统污水处理脱氮工艺过程中工艺流程复杂、处理高氨氮废水效率低等问题,利用三株不同种属的高效异养硝化-好氧反硝化细菌构建异养硝化复合菌YM,探讨其异养硝化-好氧反硝化特性及其生物强化脱氮效能研究,从而为异养硝化菌强化处理高氨氮废水工程应用提供理论依据。结果表明:异养硝化复合菌YM的增殖速率、异养氨氧化、好氧反硝化能力均优于单一菌种,YM强化后的污泥系统氨氧化速率较未强化系统从7.04 mg/L/h提高到12.2 mg/L/h,并且生物强化作用可有效提高污泥系统的抗冲击负荷能力,一定程度上提高了系统的处理能力。研究表明异养硝化菌强化污水脱氮处理具有显著的应用潜能,尤其对于目前尚缺少经济高效处理技术的高污染物浓度废水处理而言,无疑是一条具有高潜在应用价值的新途径。     

全程硝化菌微生物学特性及在水处理领域的应用潜力

全程硝化菌是近期微生物氮循环领域的重大发现之一,引发了对其全球分布、系统发育特征和生理生化特性的广泛关注。本文综述了全程硝化菌在土壤、地表水、废水处理系统等生境的分布规律及影响因子;并从底物亲和力、代谢多样性等方面阐述了其与传统硝化微生物间的竞争互作和生态位分离机制;基于上述特征提出全程硝化菌在水处理领域中的应用前景,可能与其他脱氮微生物如反硝化菌、厌氧氨氧化菌和厌氧甲烷氧化菌等耦合实现在低氨氮、低溶解氧条件下的污水深度脱氮,从而节省能耗并降低温室气体排放。未来研究应继续深入研究全程硝化菌的生理生化特性,评价其生态功能和对氮素地球化学循环的贡献,并探索其在生物水处理等领域的应用潜力。     

生物强化技术在废水脱氮中的应用

废水脱氮,主要是将污水中过量的营养物质转化为N2和N2O等排放到大气中。从市政和工业污水中脱氮最普遍,有效的方法是生物法,包括传统自养硝化-缺氧反硝化,异养硝化-好氧反硝化,短程硝化和厌氧氨氧化相结合等。目前,氮污染是个很严重的问题。从脱氮方式来说,有传统自养硝化-缺氧反硝化脱氮,异养硝化-好氧反硝化脱氮、厌氧氨氧化脱氮等。本文综述了这几种脱氮方式的生物强化技术的研究进展与实际应用,并对其发展方向进行了展望。     

季节性温度变化对CANON型潮汐流人工湿地脱氮的影响

探究了温度的季节性变化对基于亚硝化的全程自养脱氮(CANON)型潮汐流人工湿地(TFCW)脱氮性能及其微生物特性的影响。CANON型TFCW中的脱氮微生物群落在温度的季节性变化下会发生不同程度的改变,其脱氮途径及性能随之会出现周期性的波动。填料层温度在20.0 ℃以上时对TFCW脱氮性能及其中的优势脱氮菌群无显著影响,CANON作用是系统脱氮的主要途径。当填料层温度低于20.0 ℃时,厌氧氨氧化菌丰度与活性显著降低,在9.3~20.0 ℃时,亚硝酸盐氧化菌(NOB)的增殖及其活性的提高使TFCW中脱氮的主要途径由CANON作用演替为硝化/反硝化作用,系统对总氮(TN)的去除率仅为(34.8±13.0)%;在2.2~9.0 ℃时,TFCW中的厌氧氨氧化菌在受到抑制的同时仍保持着对NOB和反硝化菌群的相对竞争优势,系统脱氮重新依赖于CANON作用,其对TN的去除率为(54.8±4.8)%。该研究可为CANON型TFCW工艺的优化及工程化应用提供参考。     

Unravelling the reasons for disproportion in the ratio of AOB and NOB in aerobic granular sludge

In this study, we analysed the nitrifying microbial community (ammonium-oxidizing bacteria (AOB) and nitrite-oxidizing bacteria (NOB)) within three different aerobic granular sludge treatment systems as well as within one flocculent sludge system. Granular samples were taken from one pilot plant run on municipal wastewater as well as from two lab-scale reactors. Fluorescent in situ hybridization (FISH) and quantitative PCR (qPCR) showed that Nitrobacter was the dominant NOB in acetate-fed aerobic granules. In the conventional system, both Nitrospira and Nitrobacter were present in similar amounts. Remarkably, the NOB/AOB ratio in aerobic granular sludge was elevated but not in the conventional treatment plant suggesting that the growth of Nitrobacter within aerobic granular sludge, in particular, was partly uncoupled from the lithotrophic nitrite supply from AOB. This was supported by activity measurements which showed an approximately threefold higher nitrite oxidizing capacity than ammonium oxidizing capacity. Based on these findings, two hypotheses were considered: either Nitrobacter grew mixotrophically by acetate-dependent dissimilatory nitrate reduction (ping-pong effect) or a nitrite oxidation/nitrate reduction loop (nitrite loop) occurred in which denitrifiers reduced nitrate to nitrite supplying additional nitrite for the NOB apart from the AOB.     

Nitrite effect on ammonium and nitrite oxidizing processes in a nitrifying sludge

Nitrite accumulation can be undesirable in nitrifying reactors used for the biological elimination of nitrogen from wastewaters because the ammonium oxidation process was seen to be inhibited. There is a need to better understand the effects of nitrite on both ammonium and nitrite oxidizing processes. In this paper, the effect of nitrite on the nitrifying activity of a sludge produced in steady-state nitrification was evaluated in batch cultures. At 25 mg N/l of added nitrite, nitrification was successfully carried out. Addition of higher nitrite concentrations to nitrifying cultures (100 and 200 mg N/l) provoked inhibitory effects on the nitrification respiratory process. Nitrite at 100 and 200 mg N/l induced a significant decrease in the values for nitrate yield (−20% and −34%, respectively) and specific rate of nitrate formation (−26% and −67%, respectively), while the ammonium consumption efficiency kept high and the specific rate of ammonium oxidation did not significantly change. This showed that the nitrite oxidizing process was more sensitive to the presence of nitrite than the ammonium oxidizing process. These results showed that as a consequence of nitrite accumulation in nitrification systems, the activity of the nitrite oxidizing bacteria could be more inhibited than that of the ammonium oxidizing bacteria, provoking a higher accumulation of nitrite in the medium.     

Identification of novel small molecule enhancers of protein production by cultured mammalian cells

Shortcut nitrogen removal, that is, removal via formation and reduction of nitrite rather than nitrate, has been observed in membrane-aerated biofilms (MABs), but the extent, the controlling factors, and the kinetics of nitrite formation in MABs are poorly understood. We used a special MAB reactor to systematically study the effects of the dissolved oxygen (DO) concentration at the membrane surface, which is the biofilm base, on nitrification rates, extent of shortcut nitrification, and microbial community structure. The focus was on anoxic bulk liquids, which is typical in MAB used for total nitrogen (TN) removal, although aerobic bulk liquids were also studied. Nitrifying MABs were grown on a hollow-fiber membrane exposed to 3 mg N/L ammonium. The MAB intra-membrane air pressure was varied to achieve different DO concentrations at the biofilm base, and the bulk liquid was anoxic or with 2 g m(-3) DO. With 2.2 and 3.5 g m(-3) DO at the biofilm base, and with an anoxic bulk-liquid, the ammonium fluxes were 0.75 and 1.0 g N m(-2) day(-1), respectively, and nitrite was the main oxidized nitrogen product. However, with membrane DO of 5.5 g m(-3), and either zero or 2 g m(-3) DO in the bulk, the ammonium flux was around 1.3 g N m(-2) day(-1), and nitrate flux increased significantly. For all experiments, the cell density of ammonium oxidizing bacteria (AOB) was relatively uniform throughout the biofilm, but the density of nitrite oxidizing bacteria (NOB) decreased with decreasing biofilm DO. Among NOB, Nitrobacter spp. were dominant in biofilm regions with 2 g m(-3) DO or greater, while Nitrospira spp. were dominant in regions with less than 2 g m(-3) DO. A biofilm model, including AOB, Nitrobacter spp., and Nitrospira spp., was developed and calibrated with the experimental results. The model predicted the greatest extent of nitrite formation (95%) and the lowest ammonium oxidation flux (0.91 g N m(-2) day(-1)) when the membrane DO was 2 g m(-3) and the bulk liquid was anoxic. Conversely, the model predicted the lowest extent of nitrite formation (40%) and the highest ammonium oxidation flux (1.5 g N m(-2) day(-1)) when the membrane-DO and bulk-DO were 8 g m(-3) and 2 g m(-3), respectively. The estimated kinetic parameters for Nitrospira spp., revealed a high affinity for nitrite and oxygen. This explains the dominance of Nitrospira spp. over Nitrobacter spp. in regions with low nitrite and oxygen concentrations. Our results suggest that shortcut nitrification can effectively be controlled by manipulating the DO at the membrane surface. A tradeoff is made between increased nitrite accumulation at lower DO, and higher nitrification rates at higher DO.     

Achieving nitrite accumulation in a continuous system treating low-strength domestic wastewater: switchover from batch start-up to continuous operation with process control

Although biological nitrogen removal via nitrite is recognized as one of the cost-effective and sustainable biological nitrogen removal processes, nitrite accumulation has proven difficult to achieve in continuous processes treating low-strength nitrogenous wastewater. Partial nitrification to nitrite was achieved and maintained in a lab-scale completely stirred tank reactor (CSTR) treating real domestic wastewater. During the start-up period, sludge with ammonia-oxidizing bacteria (AOB) but no nitrite-oxidizing bacteria (NOB) was obtained by batch operation with aeration time control. The nitrifying sludge with the dominance of AOB was then directly switched into continuous operation. It was demonstrated that partial nitrification to nitrite in the continuous system could be repeatedly and reliably achieved using this start-up strategy. The ratio of dissolved oxygen to ammonium loading rate (DO/ALR) was critical to maintain high ammonium removal efficiency and nitrite accumulation ratio. Over 85% of nitrite accumulation ratio and more than 95% of ammonium removal efficiency were achieved at DO/ALR ratios in an optimal range of 4.0–6.0 mg O₂/g N d, even under the disturbances of ammonium loading rate. Microbial population shift was investigated, and fluorescence in situ hybridization analysis indicated that AOB were the dominant nitrifying bacteria over NOB when stable partial nitrification was established.     

Long-term effect of dissolved oxygen on partial nitrification performance and microbial community structure

In this study, the performance of partial nitrification via nitrite and microbial community structure were investigated and compared in two sequencing batch reactors (SBR) with different dissolved oxygen (DO) levels. Both reactors achieved stable partial nitrification with nitrite accumulation ratio of above 95% by using real-time aeration duration control. Compared with high DO (above 3 mg/l on average) SBR, simultaneous nitrification and denitrification (SND) via nitrite was carried out in low DO (0.4–0.8 mg/l) SBR. The average efficiencies of SND in high DO and low DO reactor were 7.7% and 44.9%, and the specific SND rates were 0.20 and 0.83 mg N/(mg MLSS h), respectively. Low DO did not produce sludge with poorer settling properties but attained lower turbidities of the effluent than high DO. Fluorescence in situ hybridization (FISH) analysis in both the reactors showed that ammonia-oxidizing bacteria (AOB) were the dominant nitrifying bacteria and nitrite-oxidizing bacteria (NOB) did not be recovered in spite of exposing nitrifying sludge to high DO. The morphology of the sludge from both two reactors according to scanning electron microscope indicated that small rod-shaped and spherical clusters were dominant, although filamentous bacteria and few long rod-shaped coexisted in the low DO reactor. By selecting properly DO level and adopting process control method is not only of benefit to the achievement of novel biological nitrogen removal technology, but also favorable to sludge population optimization.     

Settleability and kinetics of a nitrifying sludge in a sequencing batch reactor

A physiological study of a nitrifying sludge was carried out in a sequencing batch reactor (SBR). Pseudo steady-state nitrification conditions were obtained with an ammonium removal efficiency of 99% +/- 1% and 98% +/- 2% conversion of NH4+-N to NO3 - -N. The rate of biomass production was negligible (1.3 +/- 0.1 mg microbial protein-N.L(-1).d(-1)). The sludge presented good settling properties with sludge volume index values lower than 20 mL.g(-1) and an exopolymeric protein/carbohydrate ratio of 0.53 +/- 0.34. Kinetic results indicated that the nitrifying behavior of the sludge changed with the number of cycles. After 22 cycles, a decrease in the specific rate of NO3- -N production coupled with an increase in the NO2- -N accumulation were observed. These results showed that the activity of the nitrite oxidizing bacteria decreased at a longer operation time. Ammonia oxidizing bacteria were found to exhibit the best stability. After 4 months of operation, the specific rates of NH4+-N consumption and NO3- -N production were 1.72 NH4+-N per microbial protein-N per hour (g.g(-1).h(-1)) and 0.54 NO3- -N per microbial protein-N per hour (g.g(-1).h(-1)), respectively.     

Heterotrophic nitrification in add forest soils

Ninety cultures of heterotrophic organisms were isolated from soils of four acid Norwegian forest sites, which were active in nitrifying. The isolates were tested for ability to form nitrite in a glucose-ammonium-inorganic salts medium. Eleven cultures were found capable of oxidizing ammonium to nitrite. The nitrifying organisms consist of 4 bacteria and 7 fungi.     

Modeling and simulation of oxygen-limited partial nitritation in a membrane-assisted bioreactor (MBR)

Combination of a partial nitritation process and an anaerobic ammonium oxidation process for the treatment of sludge reject water has some general cost-efficient advantages compared to nitrification-denitrification. The integrated process features two-stage autotrophic conversion of ammonium via nitrite to dinitrogen gas with lower demand for oxygen and no external carbon requirement. A nitrifying membrane-assisted bioreactor (MBR) for the treatment of sludge reject water was operated under continuous aeration at low dissolved oxygen (DO) concentrations with the purpose of generating nitrite accumulation. Microfiltration was applied to allow a high sludge retention time (SRT), resulting in a stable partial nitritation process. During start-up of the MBR, oxygen-limited conditions were induced by increasing the ammonium loading rate and decreasing the oxygen transfer. At a loading rate of 0.9 kg N m(-3) d(-1) and an oxygen concentration below 0.1 mg DO L(-1), conversion to nitrite was close to 50% of the incoming ammonium, thereby yielding an optimal effluent within the stoichiometric requirements for subsequent anaerobic ammonium oxidation. A mathematical model for ammonium oxidation to nitrite and nitrite oxidation to nitrate was developed to describe the oxygen-limited partial nitritation process within the MBR. The model was calibrated with in situ determinations of kinetic parameters for microbial growth, reflecting the intrinsic characteristics of the ammonium oxidizing growth system at limited oxygen availability and high sludge age. The oxygen transfer coefficient (K(L)a) and the ammonium-loading rate were shown to be the appropriate operational variables to describe the experimental data accurately. The validated model was used for further steady state simulation under different operational conditions of hydraulic retention time (HRT), K(L)a, temperature and SRT, with the intention to support optimized process design. Simulation results indicated that stable nitrite production from sludge reject water was feasible with this process even at a relatively low temperature of 20 degrees C with HRT down to 0.25 days.     

Biological nitrogen removal with nitrification and denitrification via nitrite pathway

Presently, the wastewater treatment practices can be significantly improved through the introduction of new microbial treatment technologies. To meet increasingly stringent discharge standards, new applications and control strategies for the sustainable removal of ammonium from wastewater have to be implemented. Partial nitrification to nitrite was reported to be technically feasible and economically favorable, especially when wastewater with high ammonium concentrations or low C/N ratios is treated. For successful implementation of the technology, the critical point is how to maintain partial nitrification of ammonium to nitrite. Partial nitrification can be obtained by selectively inhibiting nitrite oxidizing bacteria through appropriate regulation of the system’s DO concentration, microbial SRT, pH, temperature, substrate concentration and load, operational and aeration pattern, and inhibitor. The review addressed the microbiology, its consequences for their application, the current status regarding application, and the future developments.