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1.
厌氧氨氧化菌混培物生长及代谢动力学研究1   总被引:4,自引:0,他引:4  
研究了厌氧氨氧化菌混培物的动力学特性。测得细胞产率系数1.573mgVS(mmol NH+4)-1;细胞衰减常数0.052mgVS(g·VS·d)-1。厌氧氨氧化菌混培物的最大氨氧化速率1.320~2.761mmol(gVS·d)-1,最大亚硝酸盐转化(反硝化)速率14.497mmol(gVS·d)-1。厌氧氨氧化菌混培物利用氨的Km值1.801~4.215mmol·L-1,利用亚硝酸盐的Km值0.468mmol·L-1。氨自身的抑制常数38.018~98.465mmol·L-1,实际最大氨氧化速率的氨浓度16.656mmol·L-1。亚硝酸盐对厌氧氨氧化的抑制常数5.401~11.995mmol·L-1。厌氧氨氧化的最适pH7.605。厌氧氨氧化的最适温度30℃。Vmaxa、Kma、Kia和Kin的活化能依次为37.316、30.239、33.695和30473kJ·mol-1。  相似文献   

2.
厌氧氨氧化菌富集培养物对羟胺的转化研究   总被引:1,自引:0,他引:1       下载免费PDF全文
【目的】羟胺是厌氧氨氧化的重要中间产物,本研究旨在探明厌氧氨氧化菌对羟胺的转化特性。【方法】采用厌氧氨氧化菌富集培养物,以羟胺和亚硝酸盐为基质进行分批培养试验,检测反应液中基质和产物的消涨情况。【结果】不接种厌氧氨氧化富集培养物时,羟胺和亚硝酸盐具有化学稳定性,彼此不发生化学反应;接种厌氧氨氧化富集培养物后,羟胺和亚硝酸盐发生化学反应;反应过程中有中间产物氨的产生和转化,最大氨氮积累浓度为0.338mmol/L;液相中总氮浓度从起始的4.694mmol/L降至结束时的0.812mmol/L,转化率为82.7%。羟胺和亚硝氮浓度均为2.5mmol/L时,羟胺最大比污泥转化速率为0.535mmol/(gVSS.h),是厌氧氨氧化反应体系中氨氮最大比污泥转化速率的1.81倍。将羟胺浓度提高至5.0mmol/L时,羟胺和亚硝氮转化速率分别提高26.7%和120.7%,最大氨氮积累浓度为0.795mmol/L;将亚硝氮浓度提高至5.0mmol/L时,羟胺和亚硝氮转化速率分别提高6.9%和9.0%,最大氨氮积累浓度为1.810mmol/L。【结论】厌氧氨氧化富集培养物能够转化羟胺,其对羟胺的转化速率高于对氨的转化速率。羟胺相对过量可显著加快羟胺和亚硝酸盐的转化速率,亚硝酸盐相对过量对羟胺和亚硝氮转化速率影响不大,提高羟胺或亚硝氮浓度均会增大中间产物氨氮的积累。实验现象可用van de Graaf模型解释,对于进一步开发厌氧氨氧化工艺具有重要的理论意义。  相似文献   

3.
以城市污水处理工程的好氧活性污泥为菌源,通过富集、分离纯化,筛选出一株自养型氨氧化细菌CM-NRO14,进一步研究了该菌株的系统发育地位及氨氧化特性。根据菌株的形态学特征、生理生化特性及16S rDNA序列测定分析,确定该菌株属于亚硝酸单胞杆菌。CM-NRO14菌株的最大氨氧化速率24.54 mg/(L·d),利用氨的Km值45.66 mg/L,氨自身的抑制常数2401 mg/L,最大氨氧化速率的氨浓度331.2 mg/L。亚硝酸盐对氨氧化的抑制常数1524 mg/L。氨氧化的最适pH 7.79。氨氧化的最适温度34℃。菌株在初始氨氮浓度为180 mg/L,最佳氨氧化pH、温度条件下,4 d内氨氮降解率达到91.6%,菌株倍增时间2.94 d。  相似文献   

4.
研究了基因工程菌 1 0 1 6所产的氨基酰化酶的酶学特性。该酶的拆分速率符合米氏方程 ,且在 0 .5mol/L的高底物浓度下 ,无底物抑制现象。 37℃时的米氏常数和最大反应速率分别为 0 .0 4 8mmol/L和 2 .1 78mmol/L·h。最适反应温度为 5 5℃。5 5℃时 ,Km为 0 .0 37mmol/L ,Vmax为 2 .5 5 8mmol/L·h。最适底物为乙酰蛋氨酸 ;热稳定性好。  相似文献   

5.
一株反硝化细菌的鉴定及其厌氧氨氧化能力的证明   总被引:3,自引:0,他引:3  
从厌氧氨氧化反应器中分离获得了反硝化细菌D3菌株. 综合其外部形态特性、生理生化特性、VitekGN检测结果、Biolog碳源利用特性, 以及菌株的(G+C)%(mol/mol)含量和系统发育分析, 将它归入门多萨假单胞菌(Pseudomonas mendocina). 该菌株是典型的反硝化细菌, 具有较强的反硝化活性, 当硝酸盐浓度为88.5 mg/L时, 反硝化速率最大, 为26.2 mg/(L·d). 最适生长pH为7.84, 最适生长温度为34.9℃. 该菌株显现较强的厌氧氨氧化能力, 对硝酸盐的最大利用速率为6.37 mg/(L·d), 对氨的最大利用速率为3.34 mg/(L·d), 消耗的氨氮和硝酸盐氮之比为1︰1.91. 该菌株可产生特殊的细胞结构, 与厌氧氨氧化密切相关, 推测这一特殊细胞结构可能是进行厌氧氨氧化的厌氧氨氧化体. 证明了反硝化细菌具有厌氧氨氧化活性, 扩大了厌氧氨氧化菌的种群范围, 为深入研究厌氧氨氧化菌及其在全球氮素循环中的贡献和进一步开发厌氧氨氧化工艺打下了良好的基础.  相似文献   

6.
从氧化葡萄糖酸杆菌(Gluconobacter oxydans)的基因组DNA上扩增出木糖醇脱氢酶基因xdh,构建了诱导型表达载体pSE-xdh,导入E.coli JM109后获得了高效表达木糖醇脱氢酶基因的重组菌JM109/pSE-xdh。通过HisTrap HP亲和层析和SephacrylS 300分子筛两步纯化从细胞中得到纯酶,并对酶学性质进行研究。XDH最适还原反应的pH值为5.0,最适还原反应的温度为35℃;最适氧化反应的pH值为11.0,最适氧化反应的温度为30℃。重组菌中的XDH依赖NADH,对NADH的米氏常数Km=57.8 mmol/L,最大反应速率Vmax=1209.1 mmol/(ml·min)。重组菌的XDH酶活力为13.9 U/mg。利用重组菌和原始菌混合静止细胞转化D 木酮糖,16 h 28.0 g/L D木酮糖生成16.7 g/L木糖醇,而原始菌单独转化只生成8.3 g/L木糖醇。  相似文献   

7.
中试厌氧氨氧化反应器的启动与调控   总被引:17,自引:1,他引:16  
研究了中试厌氧氨氧化(Anaerobic ammonium oxidation,Anammox)反应器的启动性能。结果表明,以硝化反硝化污泥、短程硝化污泥、厌氧絮体污泥和厌氧颗粒污泥混合接种,经过255d的运行,可在常温下(5oC~27oC)成功启动中试Anammox反应器,反应器的基质氮去除速率可达1.30kg/(m3·d)。厌氧氨氧化是致碱反应,厌氧氨氧化成为反应器内的主导反应后,进水pH宜控制在厌氧氨氧化适宜范围的偏低水平(6.8左右)。亚硝酸盐既是Anammox菌的基质,也是抑制剂,控制进水亚硝酸盐浓度(13~36mg/L)有助于厌氧氨氧化反应。菌种是生物反应器的功能之源,向中试装置投加少量厌氧氨氧化污泥(投加比2%),可大大加速中试Anammox反应器的启动进程。  相似文献   

8.
厌氧氨氧化菌群体感应系统研究   总被引:6,自引:0,他引:6  
丁爽  郑平  张萌  陆慧锋 《生态学报》2012,32(8):2581-2587
厌氧氨氧化(Anammox)是以铵为电子供体将亚硝酸盐转化为氮气的生物过程。厌氧氨氧化菌(AAOB)生理代谢和细胞结构均十分特殊,且在氮素循环中起着十分重要的作用。厌氧氨氧化已成为环境学、微生物学、海洋学等领域的研究热点。但是,至今人们未能对厌氧氨氧化菌进行纯培养,这严重限制了对厌氧氨氧化菌的深入研究。群体感应是一种普遍存在于微生物细胞之间的通讯机制,它具有根据菌群密度和周围环境变化调节基因表达,以控制细菌群体行为的功能。厌氧氨氧化菌活性的细胞密度效应和生物团聚行为与细菌中普遍存在的群体感应现象相符。探讨了厌氧氨氧化菌群体感应系统存在的可能性、工作机制及其生态学意义,以期为厌氧氨氧化菌的分离培养、团聚体培育等提供理论指导。  相似文献   

9.
高效反硝化菌aHD7的筛分、脱氮特性及厌氧氨氧化性   总被引:1,自引:0,他引:1  
从活性污泥中筛选出一株高效反硝化菌aHD7,30℃静置培养3d,脱氮率可达91.7%,且反应过程中亚硝酸盐积累量较低,3d后亚硝酸盐氮浓度基本稳定在1.8mg.L-1.显微镜观察显示,菌株为革兰氏阴性杆菌,大小为0.5 μm×(1.5~2.5) μm.通过生理生化特性及16S rDNA同源性分析,初步推断该菌株为门多萨假单胞菌(Pseudomonas mendocina).考察了碳源、C/N、氮初始浓度、pH等因素对菌株反硝化性能的影响.结果表明:对中低浓度硝酸盐(硝酸盐氮浓度≤276.95 mg.L-1),脱氮率接近100%,硝酸盐氮浓度高达553.59 mg·L-1时,脱氮率可达66.8%,且亚硝酸盐积累量甚微;最适碳源为乙醇;C/N为6~8和偏中性条件有利于反硝化反应.aHD7具有较强的厌氧氨氧化性,平均氨利用率达4.56 mg·L-1·d-1.  相似文献   

10.
从Burkholderiacepecianjut1分离纯化N氨甲酰D氨基酸水解酶(NDase)。实验表明,该酶亚基35KD,最适温度为52℃,最适pH为7.2左右。以N氨甲酰D苯丙氨酸作底物,其米氏常数Km为10.22mmol/L,最大反应速度Vmax为0.27mmol/(L·min)。实验表明二价金属离子对酶活有重要影响。  相似文献   

11.
气提式内循环硝化反应器运行性能的研究   总被引:25,自引:1,他引:24  
气提式内循环反应器具有很好的生物硝化性能,能承受高进水氨浓度(78.49mmol/L),具有高容积转化效率(163.18 mmol/L·d),运行性能稳定(氨去除率保持在94.42%以上)。在气提式内循环反应器的运行过程中,可产生硝化颗粒污泥。颗粒污泥开始出现的时间约为45d,颗粒污泥的粒径平均值0.83 mm,沉降速度55.53m/h,氨氧化活性0.95mmol (NH+4-N)/g(VS)·d。硝化颗粒污泥也具有厌氧氨氧化活性,氨氧化速率0.23mmol (NH+4-N)/g(VS)·d,亚硝酸还原速率0.24mmol (NO-2-N)/g(VS)·d。  相似文献   

12.
Photoinactivation of Ammonia Oxidation in Nitrosomonas   总被引:4,自引:1,他引:3       下载免费PDF全文
Photoinactivation of ammonia oxidation in cells of Nitrosomonas was shown to follow first-order kinetics with a rate constant proportional to incident light intensity. The action spectrum for photoinactivation consisted of a broad peak in the ultraviolet range, where both hydroxylamine and ammonia oxidation were affected, and a shoulder at approximately 410 nm where only ammonia oxidation was affected. In photoinactivated cells, hydroxylamine but not ammonia was oxidized to nitrite and hydroxylamine but not ammonia caused reduction of cytochromes in vivo. The amount per cell of the following constituents was not measurably altered by photoinactivation: cytochromes b, c, a, and P460; ubiquinone; phospholipid; free amino acids; hydroxylamine-dependent nitrite synthetase; nitrite reductase; p-phenylenediamine oxidase; and cytochrome c oxidase. Malonaldehyde or lipid peroxides were not detected in photoinactivated cells. Photoinactivation was prevented (i) under anaerobic conditions, (ii) in the presence of methanol, allylthiourea, thiosemicarbazide, hydroxylamine, ethylxanthate, or CO at concentrations wich caused 100% inhibition of ammonia oxidation, and (iii) at concentrations of ammonia or hydroxylamine which gave a rapid rate of nitrite production. Recovery of ammonia oxidation activity in 90% inactivated cells took place in 6 h, required an energy and/or nitrogen source, and was inhibited by 400 mug of chloramphenicol per ml.  相似文献   

13.
The anaerobic ammonia-oxidizing activity of the planctomycete Candidatus "Brocadia anammoxidans" was not inhibited by NO concentrations up to 600 ppm and NO2 concentrations up to 100 ppm. B. anammoxidans was able to convert (detoxify) NO, which might explain the high NO tolerance of this organism. In the presence of NO2, the specific ammonia oxidation activity of B. anammoxidans increased, and Nitrosomonas-like microorganisms recovered an NO2-dependent anaerobic ammonia oxidation activity. Addition of NO2 to a mixed population of B. anammoxidans and Nitrosomonas induced simultaneous specific anaerobic ammonia oxidation activities of up to 5.5 mmol of NH4+ g of protein(-1) h(-1) by B. anammoxidans and up to 1.5 mmol of NH4+ g of protein(-1) h(-1) by Nitrosomonas. The stoichiometry of the converted N compounds (NO2-/NH3 ratio) and the microbial community structure were strongly influenced by NO2. The combined activity of B. anammoxidans and Nitrosomonas-like ammonia oxidizers might be of relevance in natural environments and for technical applications.  相似文献   

14.
一株氨氧化链霉菌的分类鉴定及其氨氧化特性的研究   总被引:2,自引:0,他引:2  
从硝化反应器中分离获得一株链霉菌。根据其形态特征、培养特征、生理生化特性,(G+C)mol%含量以及16S rDNA序列和DNA杂交结果,将其归入链霉菌属中的比基尼链霉菌(Streptomycesbikiniensis)。该菌株既能在YD培养基上异养生长,也能在无机培养基上自养生长,异养生长速率(Vmax为0.39mg/L\5d)明显高于自养生长速率(Vmax为0.22mg/L.d)。异养生长时,氨氮主要用于合成细胞物质;自养生长时,部分氨氮用于合成细胞物质,部分氨氮转化成亚硝酸盐。在无机培养基上自养生长时,最适氨浓度为118mgN/L。最适生长pH值为9.36,最适氨氧化pH值为9.29。最适生长温度为31℃,最适氨氧化温度为40.6℃。提高溶解氧浓度有利于该菌株生长和氨氧化,菌体生长对溶解氧浓度的敏感性高于氨氧化。  相似文献   

15.
Optimal operational factors for nitrite accumulation in batch reactors   总被引:12,自引:0,他引:12  
Bae W  Baek S  Chung J  Lee Y 《Biodegradation》2001,12(5):359-366
The environmental factors that affected the accumulation of nitrite in nitrifying reactors were investigated using a mixed culture. A batch reactor with 50 mg-N/l of ammonia was used. The pH, temperature and dissolved oxygen concentration were varied. The concentration of unionized free ammonia also changed with the oxidation of ammonia and the variation of pH and temperature. The accumulation of nitrite was affected sensitively by pH and temperature. A higher nitrite concentration was observed at pH 8-9 or temperature around 30 °C. The dissolved oxygen also affected, giving the highest nitrite accumulation at around 1.5 mg/l. These were the favoredconditions for nitrite production. The free ammonia concentration influenced thenitrite accumulation also, by inhibiting nitrite oxidation. The inhibition becameapparent at a concentration of approximately 4 mg/l or above, but insignificant atbelow 1 mg/l. Thus, simultaneously high free ammonia concentration and maximumspecific ammonia-oxidation rate (above 15 × 10-3 mg-N/mg-VSSh)were needed for a significant nitrite accumulation. When the two conditions were met, thenthe highest accumulation was observed when the ratio of the maximum specific oxidationrate of ammonia to the maximum specific oxidation rate of nitrite (ka/kn) was highest.Under the optimal operating conditions of pH 8, 30 °C and 1.5 mg/l of dissolvedoxygen, as much as 77% of the removed ammonia accumulated in nitrite.  相似文献   

16.
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.  相似文献   

17.
Studies on the oxidation of ammonia by Nitrosomonas   总被引:2,自引:0,他引:2       下载免费PDF全文
1. Free-energy calculations for pH7 showed that the oxidation of ammonia to hydroxylamine is endergonic and that the oxidations of hydroxylamine to nitrite and hydrazine to nitrogen are exergonic. It is suggested that the oxidation of ammonia requires the expenditure of energy. 2. The anaerobic dehydrogenation of hydrazine to nitrogen by extracts of the autotrophic nitrifying micro-organism, Nitrosomonas, in the presence of methylene blue as electron acceptor, was less rapid than the anaerobic dehydrogenation of hydroxylamine to nitric oxide. The inhibition by hydrazine of the dehydrogenation of hydroxylamine was attributed to substrate competition. 3. Whole cells in air did not produce nitrite from hydrazine. They produced nitrite from low concentrations of hydroxylamine more rapidly than from equimolar concentrations of ammonia; this result is consistent if hydroxylamine is an intermediate of the oxidation of ammonia. 4. The production of nitrite from hydroxylamine by whole cells was slightly inhibited by hydrazine, but the production of nitrite from ammonia was greatly inhibited and small amounts of hydroxylamine were formed. These results suggested that the dehydrogenation of hydroxylamine supplied energy required for the oxidation of ammonia and that hydroxylamine appeared because the energy production was replaced by that of the dehydrogenation of hydrazine. 5. The oxidation of hydroxylamine by whole cells was not inhibited by thiourea, but micromolar concentrations of the metal-binding agent markedly inhibited the oxidation of ammonia to hydroxylamine, suggesting that the oxidation of ammonia involved copper. A possible mechanism for the activation of ammonia is suggested.  相似文献   

18.
In wastewater treatment plants with anaerobic sludge digestion, 15-20% of the nitrogen load is recirculated to the main stream with the return liquors from dewatering. Separate treatment of this ammonium-rich digester supernatant would significantly reduce the nitrogen load of the activated sludge system. Some years ago, a novel biological process was discovered in which ammonium is converted to nitrogen gas under anoxic conditions with nitrite as the electron acceptor (anaerobic ammonium oxidation, anammox). Compared to conventional nitrification and denitrification, the aeration and carbon-source demand is reduced by over 50 and 100%, respectively. The combination of partial nitritation to produce nitrite in a first step and subsequent anaerobic ammonium oxidation in a second reactor was successfully tested on a pilot scale (3.6 m(3)) for over half a year. This report focuses on the feasibility of nitrogen removal from digester effluents from two different wastewater treatment plants (WWTPs) with the combined partial nitritation/anammox process. Nitritation was performed in a continuously stirred tank reactor (V=2.0 m(3)) without sludge retention. Some 58% of the ammonium in the supernatant was converted to nitrite. At 30 degrees C the maximum dilution rate D(x) was 0.85 d(-1), resulting in nitrite production of 0.35 kg NO(2)-N m(-3)(reactor) d(-1). The nitrate production was marginal. The anaerobic ammonium oxidation was carried out in a sequencing batch reactor (SBR, V=1.6 m(3)) with a nitrogen elimination rate of 2.4 kg N m(-3)(reactor) d(-1) during the nitrite-containing periods of the SBR cycle. Over 90% of the inlet nitrogen load to the anammox reactor was removed and the sludge production was negligible. The nitritation efficiency of the first reactor limited the overall maximum rate of nitrogen elimination.  相似文献   

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Hydroxylamine oxidoreductase (HAO) from the ammonia-oxidizing bacterium Nitrosomonas europaea normally catalyzes the four-electron oxidation of hydroxylamine to nitrite, which is the second step in ammonia-dependent respiration. Here we show that, in the presence of methyl viologen monocation radical (MV(red)), HAO can catalyze the reduction of nitric oxide to ammonia. The process is analogous to that catalyzed by cytochrome c nitrite reductase, an enzyme found in some bacteria that use nitrite as a terminal electron acceptor during anaerobic respiration. The availability of a reduction pathway to ammonia is an important factor to consider when designing in vitro studies of HAO, and may also have some physiological relevance. The reduction of nitric oxide to ammonia proceeds in two kinetically distinct steps: nitric oxide is first reduced to hydroxylamine, and then hydroxylamine is reduced to ammonia at a tenfold slower rate. The second step was investigated independently in solutions initially containing hydroxylamine, MV(red), and HAO. Both steps show first-order dependence on nitric oxide and HAO concentrations, and zero-order dependence on MV(red) concentration. The rate constants governing each reduction step were found to have values of (4.7 +/- 0.3) x 10(5) and (2.06 +/- 0.04) x 10(4) M(-1) s(-1), respectively. A second reduction pathway, with second-order dependence on nitric oxide, may become available as the concentration of nitric oxide is increased. Such a pathway might lead to production of nitrous oxide. We estimate a maximum value of (1.5 +/- 0.05) x 10(10) M(-2) s(-1) for the rate constant of the alternative pathway, which is small and suggests that the pathway is not physiologically important.  相似文献   

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