好氧反硝化生物脱氮技术的研究进展

好氧反硝化生物脱氮技术自提出以来,凭借能实现同步硝化反硝化、节省基建投资及运行费用等诸多优点,受到国内外环境领域学者的广泛关注。本文首先总结了近年来好氧反硝化菌种的筛选分离情况,以及环境因子对好氧反硝化菌脱氮效能的影响,包括溶解氧(dissolved oxygen,DO)、碳氮比(C/N)、温度等。然后深入探讨了好氧反硝化生物脱氮技术的原理,好氧反硝化过程中的关键功能基因及酶,同时介绍了分子生物技术在好氧反硝化研究过程中的应用,以及好氧反硝化生物脱氮技术在实际应用方面的研究现状。最后,基于目前的研究瓶颈问题,对未来好氧反硝化生物脱氮技术的研究方向提出了科学展望。     

关于好氧反硝化菌筛选方法的研究

采用污泥驯化手段富集好氧反硝化细菌,将得到的驯化污泥分离纯化,共得到105株菌。用测TN的方法对所筛菌株进行初筛,得到25株对TN去除率达到50％以上的菌株。用氮元素轨迹跟踪测定法复筛,证实这25株菌都可以在好氧条件下进行硝酸盐呼吸,其中24株菌的反硝化过程为：NO3^-N→NO2^-N→N2,研究中还发现在反硝化过程中硝酸盐和亚硝酸盐不存在明显竞争被利用的作用。同时还提出了可能实现短程同步硝化反硝化以及在反馈作用的调节下,加快硝化反应速度的观点。     

异养硝化-好氧反硝化细菌的研究进展

异养硝化-好氧反硝化菌株的发现是对传统硝化反硝化的突破和发展。近年来由于其独特的生物学特性及其在污水处理中的巨大优势,受到众多学者的青睐。文章介绍了异养硝化-好氧反硝化菌的筛选,异养硝化-好氧反硝化代谢途径和异养硝化-好氧反硝化菌的影响因素,并总结了异养硝化-好氧反硝化菌在废水处理中的研究进展,最后展望未来研究的方向。     

SBR和MBR反应器中好氧反硝化菌的筛选与分析

好氧反硝化菌是土壤、沉积物、活性污泥等介质中广泛存在的一类微生物。研究以相同种泥扩大培养的SBR(序批式活性污泥反应器)和MBR(膜生物反应器)中活性污泥为研究对象,采用平板分离法分别从运行6个月的SBR和MBR反应器中分离得到9株和11株好氧反硝化菌。经好氧反硝化性能测定发现,20株细菌中有16株总氮去除率在50%以上,且NO_2~--N累积量均在0.5 mg/L以下。经系统进化分析表明,在门分类级别中,采用同一种泥的2个反应器中好氧反硝化菌表现出极大的一致性,20株好氧反硝化菌全部属于变形菌门(Proteobacteria)。但是,进一步分析发现不同反应器中好氧反硝化菌表现出较大的属、种间的差异。其中,SBR反应器9株好氧反硝化菌分属于4个属,6个物种;而从MBR反应器获得的11株细菌分属于2个属,6个物种;仅1个物种(Pseudomonas toyotomiensis)在2个反应器均有发现。     

好氧反硝化菌代谢机制及其与重金属相互作用的代谢特征

好氧反硝化是在好氧条件下将NO3–-N最终转化为N2的过程。好氧反硝化菌不仅表现出优秀的脱氮性能,可在许多极端条件下生存,还拥有多种重金属耐受性。本文总结了不同重金属Cr(VI)、Cu(II)和Cd(II)对好氧反硝化菌脱氮效率的影响,同时整理了好氧反硝化菌对不同重金属的耐受或去除机制。分析了好氧反硝化菌在工业废水处理中的应用潜力,最后对好氧反硝化菌的未来研究方向进行了简要的展望,期望为工业废水中氮污染和重金属污染处理提供更加全面的理论认识和技术支持。     

异养硝化-好氧反硝化菌脱氮相关酶系及其编码基因的研究进展

水体氮素污染日益严重,如何经济、高效地去除水体氮素已成为研究热点。近年来,研究人员已从不同环境中分离到许多同时具有异养硝化和好氧反硝化功能的菌株,此类菌生长迅速,可在好氧条件下同时实现硝化和反硝化的过程,并可用于脱除有机污染物,是一类应用潜力巨大的脱氮菌。目前,异养硝化-好氧反硝化菌的脱氮途径和机制主要是通过测定氮循环中间产物或终产物、测定相关酶活性、注释部分氮循环相关基因及参考自养硝化菌和缺氧反硝化菌的氮循环途径等进行研究,其完整的氮素转化途径和氮代谢机制还需要进一步明确。总结了目前异养硝化-好养反硝化菌的脱氮相关酶系及其编码基因的研究进展,以期为异养硝化-好氧反硝化菌的理论研究及其在污水脱氮处理上的应用提供参考。     

异养硝化细菌脱氮特性及研究进展

异养硝化细菌能够在利用有机碳源生长的同时将含氮化合物硝化生成羟胺、亚硝酸盐、硝酸盐等产物, 多数还能同时进行好氧反硝化作用, 直接将硝化产物转化为含氮气体。因此, 这类细菌已成为废水处理中生物脱氮新工艺的重要研究对象。本文综述了目前所分离出的一些异养硝化菌的脱氮特性, 分析了各种环境条件如温度、pH、溶解氧、碳源类型、C/N以及抑制剂等对异养硝化菌的影响, 并介绍了异养硝化菌的应用现状及前景。     

海洋环境异养硝化-好氧反硝化菌的研究进展

异养硝化-好氧反硝化（heterotrophic nitrifying-aerobic denitrification,HN-AD）菌的发现打破了传统的脱氮理论,可以在有氧条件下同时进行硝化和反硝化,成为近年来的研究热点。HN-AD细菌在海洋氮循环中发挥着重要作用。本文对海洋环境中HN-AD菌的多样性和部分已知氮代谢途径及相关酶系进行了介绍,分析了盐度、碳氮比、溶解氧、pH等环境因素对HN-AD菌脱氮效果的影响,对其工艺和技术应用、前景和发展方向进行了综述和展望。     

好氧反硝化微生物学机理与应用研究进展

近年来,关于好氧反硝化过程的研究主要集中在三个方面:分别是好氧反硝化菌株的分离和脱氮性能表征,好氧反硝化微生物的应用潜力分析,以及好氧反硝化过程的机理研究。好氧反硝化菌株分布范围广泛,可从多种环境中分离得到,种属以Pseudomonas sp.、Alcaligenes sp.和Paracoccus sp.为主。好氧反硝化菌株及菌群在实验室条件下表现出优良的耐冷、耐盐特性,并具有可降解毒性有机物及N_2O减排的潜力。关于好氧反硝化过程的机理研究表明,虽然硝酸盐作为电子受体的竞争力比氧气弱,但反硝化作为辅助电子传递途径,可提高产能效率,防止NAD(P)H的过量积累。因此,硝酸盐可与氧气同时参与微生物的新陈代谢,即发生好氧反硝化现象。未来除了继续分离更新更好的好氧反硝化菌株外,应加强对好氧反硝化机理及实际生物强化方面的研究。     

异养硝化-好氧反硝化的研究进展

近年来,异养硝化-好氧反硝化菌的发现打破了传统硝化反硝化理论,其在去除氮素和有机污染物的同时,能够实现同时硝化反硝化(SND),因此受到广泛关注。文章介绍了异养硝化-好氧反硝化菌的影响因素和一些已筛选菌的最佳脱氮效果,及其与传统硝化反硝化菌作用酶系的不同,列出了一些已筛选菌的氮代谢途径,并对中间产物NO2--N积累和复合菌方面的研究进展进行了综述,最后提出了异养硝化-好氧反硝化在生物强化应用中的研究现状和面临的挑战。     

好氧反硝化细菌碳氮代谢特点及途径的研究进展

好氧反硝化作用的发现打破了反硝化只能在严格厌氧条件下进行的传统认知,为生物脱氮提供了一条新的途径,已成为近些年的研究热点。碳源可为好氧反硝化过程提供能量和电子供体,其代谢难易程度直接影响着好氧反硝化细菌的脱氮效率,因此有必要明确碳源在好氧反硝化脱氮过程中的代谢机理。基于此,本文阐述了好氧反硝化细菌的种类及其对硝态氮与亚硝态氮的代谢途径;系统分析了不同好氧反硝化细菌对碳氮源代谢的差异与代谢机理;综合分析了碳代谢差异对好氧反硝化脱氮过程的影响,并对未来的研究方向进行了展望,旨在深入理解好氧反硝化细菌同时去除碳氮的机理,为提高废水生物脱氮除碳效率提供理论依据。     

好氧反硝化菌的研究进展

综述了好氧反硝化菌的种类和特性、好氧反硝化菌的反硝化作用机制和影响因素.好氧反硝化菌主要包括假单胞菌属(Pseudomonas)、产碱杆菌属(Alcaligenes)、副球菌属(Para-coccus)和芽孢杆菌属(Bacillus)等,属好氧或兼性好氧异养微生物.好氧反硝化菌能在好氧条件下进行反硝化,其主要产物是N2O,并可将铵态氮直接转化成气态产物.催化好氧反硝化菌反硝化作用的硝酸盐还原酶是周质酶而不是膜结合酶.溶解氧和C/N往往是影响好氧反硝化菌反硝化作用的主要因素.介绍了间歇曝气法、选择性培养基法等好氧反硝化菌的主要分离筛选方法.概述了好氧反硝化菌在水产养殖、废水生物处理、降解有机污染物以及对土壤氮素损失的影响方面的研究进展.     

基于响应面法对一株好氧反硝化菌脱氮效能优化

【目的】水体富营养化是当今我国水环境面临的重大水域环境问题,氮素超标排放是主要的引发因素之一。好氧反硝化菌构建同步硝化反硝化工艺比传统脱氮工艺优势更大。获得高效的好氧反硝化菌株并通过生长因子优化使脱氮效率达到最高。【方法】经过序批式生物反应器(Sequencing batch reactor,SBR)的定向驯化,筛选获得高效好氧反硝化菌株,采用响应面法优化好氧反硝化过程影响总氮去除效率的关键因子(碳氮、溶解氧、pH、温度)。【结果】从运行稳定的SBR反应器中定向筛选高效好氧反硝化菌株Pseudomonas T13,采用响应面法对碳氮比、pH和溶解氧关键因子综合优化获得在18 h内最高硝酸盐去除率95%,总氮去除率90%。该菌株的高效反硝化效果的适宜温度范围为25?30 °C;最适pH为中性偏碱;适宜的COD/NO3?-N为4:1以上;最佳溶解氧浓度在2.5 mg/L。【结论】从长期稳定运行的SBR反应器中筛选获得一株高效好氧反硝化菌Pseudomonas T13,硝酸盐还原酶比例占脱氮酶基因的30%以上,通过运行条件优化获得硝氮去除率达到90%以上,对强化废水脱氮工艺具有良好应用价值。     

Simultaneous nitrification,denitrification, and phosphorus removal in a lab-scale sequencing batch reactor

Simultaneous nitrification and denitrification (SND) via the nitrite pathway and anaerobic-anoxic-enhanced biological phosphorus removal (EBPR) are two processes that can significantly reduce the energy and COD demand for nitrogen and phosphorus removal. The combination of these two processes has the potential of achieving simultaneous nitrogen and phosphorus removal with a minimal requirement for COD. A lab-scale sequencing batch reactor (SBR) was operated in alternating anaerobic-aerobic mode with a low dissolved oxygen (DO) concentration (0.5 mg/L) during the aerobic period, and was demonstrated to accomplish nitrification, denitrification, and phosphorus removal. Under anaerobic conditions, COD was taken up and converted to polyhydroxyalkanoates (PHAs), accompanied by phosphorus release. In the subsequent aerobic stage, PHA was oxidized and phosphorus was taken up to <0.5 mg/L by the end of the cycle. Ammonia was also oxidized during the aerobic period, but without accumulation of nitrite or nitrate in the system, indicating the occurrence of simultaneous nitrification and denitrification. However, off-gas analysis showed that the final denitrification product was mainly nitrous oxide (N(2)O), not N(2). Further experimental results demonstrated that nitrogen removal was via nitrite, not nitrate. These experiments also showed that denitrifying glycogen-accumulating organisms (DGAOs), rather than denitrifying polyphosphate-accumulating organisms (DPAOs), were responsible for the denitrification activity.     

Aerobic denitrification by novel isolated strain using NO-₂-N as nitrogen source

Biological denitrification reaction can be achieved under aerobic environment. Few aerobic denitrifiers using nitrite as sole nitrogen source were identified. Using nitrite as the sole nitrogen source, this work assessed the denitrification activity of yy7, an aerobic heterotrophic denitrifier identified as Pseudomonas sp. (94% similarity) by 16S rRNA sequencing analysis. The logistic equation describes the cell growth curve, yielding a generation time of 2.9h at an initial 18 mg l(-1)NO(-)?-N. Reduction of NO(-)?-N was primarily achieved during its logarithmic growth phase, and was accompanied by an increase in suspension pH and near complete consumption of dissolved oxygen. Three genes relating to nirK, norB, and nosZ were noted to involve in isolate strain. Isolate yy7 can survive and remove up to 40 mg l(-1)NO(-)?-N and, hence, can be applied as an effective aerobic denitrifier during simultaneous nitrification and denitrification via nitrite processes.     

Effect of oxic and anoxic conditions on nitrous oxide emissions from nitrification and denitrification processes

A lab-scale sequencing batch reactor fed with real municipal wastewater was used to study nitrous oxide (N(2)O) emissions from simulated wastewater treatment processes. The experiments were performed under four different controlled conditions as follows: (1) fully aerobic, (2) anoxic-aerobic with high dissolved oxygen (DO) concentration, (3) anoxic-aerobic with low DO concentration, and 4) intermittent aeration. The results indicated that N(2)O production can occur from both incomplete nitrification and incomplete denitrification. N(2)O production from denitrification was observed in both aerobic and anoxic phases. However, N(2)O production from aerobic conditions occurred only when both low DO concentrations and high nitrite concentration existed simultaneously. The magnitude of N(2) O produced via anoxic denitrification was lower than via oxic denitrification and required the presence of nitrite. Changes in DO, ammonium, and nitrite concentrations influenced the magnitude of N(2)O production through denitrification. The results also suggested that N(2)O can be produced from incomplete denitrification and then released to the atmosphere during aeration phase due to air stripping. Therefore, biological nitrogen removal systems should be optimized to promote complete nitrification and denitrification to minimize N(2)O emissions.     

Nitrification and denitrification by Thiosphaera pantotropha in aerobic chemostat cultures

Abstract: Thiosphaera pantotropha has been reported to denitrify aerobically and nitrify heterotrophically. However, recent evidence has indicated that these properties (particularly aerobic denitrification) have been lost. The occurrence and levels of aerobic denitrification and heterotrophic nitrification by T. pantotropha in chemostat cultures have therefore been re-evaluated. Only low nitrate reduction rates were observed: the apparent nitrogen loss was of the same order of magnitude as the combined error in the calculated nitrogen consumption. However, ¹⁵N mass spectrometry revealed low aerobic denitrification rates (about 10% of the rates originally published by this group). Heterotrophic nitrification rates were about a third of previous observations. N₂ and N₂O were both produced from NH₄⁺, NO₃⁻ and NO₂⁻. Periplasmic nitrate reductase was present in aerobically grown cells.     

一株耐盐的卓贝儿氏菌(Zobellella sp.)的分离鉴定及其硝酸盐还原能力

【背景】好氧反硝化是指在有氧条件下进行反硝化作用,使得硝化和反硝化过程能够在同一反应器中同时发生,是废水脱氮最具竞争力的技术。红树林湿地中蕴藏着丰富的微生物资源,分布着大量好氧反硝化微生物。【目的】了解耐盐微生物的脱氮机制,为含盐废水生物脱氮的工程实践提供理论依据,对一株分离于红树林湿地中的耐盐好氧细菌A63的硝酸盐异化还原能力进行分析。【方法】利用形态学特征及16S rRNA基因序列测定分析,对其种属进行了鉴定,采用单因子实验测定该菌在不同环境因子下的硝酸盐还原能力,并对其反硝化脱氮条件进行了优化。【结果】初步判定该菌株为卓贝儿氏菌(Zobellellasp.),其能在盐度0%-10%、pH5.0-10.0、温度20-40°C范围内进行反硝化脱氮和硝酸盐异化还原为氨(dissimilatorynitratereductiontoammonium,DNRA)作用。菌株A63最适生长碳源为柠檬酸钠(1.2 g/L),适宜脱氮盐度为3%、pH 7.0-7.5、温度30-35°C,且C/N为10。在最适脱氮条件下,该菌株12h内能将培养基中208.8mg/L硝态氮降至0,且仅有少量铵态氮生成,无亚硝态氮积累,脱氮率高达99%。此外,该菌株在高盐度、低C/N比、弱酸性和低温等不利生境中DNRA作用显著。【结论】细菌A63生长范围宽,脱氮效率显著,适用于海水养殖废水处理。研究为今后开发高效含盐废水生物脱氮工艺奠定了基础,对于加深氮素转化规律的认识、丰富生物脱氮理论有着重要意义。     

Production of nitrogen oxide and dinitrogen oxide by autotrophic nitrifiers

Autotrophic nitrifiers have been shown to produce nitrogen oxide and dinitrogen oxide under oxic conditions. Dinitrogen oxide is produced mainly during nitrite reduction (i.e. aerobic denitrification) whereas nitrogen oxide is produced during both aerobic denitrification and as a result of chemodenitrification. Oxygen is the single most influential environmental factor affecting the production of nitrogen and dinitrogen oxides; a decrease in oxygen can result in a several-fold increase in nitrogen oxide and dinitrogen oxide production. Emission of nitrogen oxide and dinitrogen oxide from wastewater treatment plants and fertilized soils is well documented; however, only recently have the contributions from such environments to the global nitrogen and dinitrogen oxide budget been considered.