曝气生物滤池处理城镇污水厂尾水的强化脱氮及微生物群落特征分析

为优化曝气生物滤池在城镇污水厂尾水深度处理条件, 采用比较方法研究了曝气量、水力停留时间以及硝化液回流等参数对曝气生物滤池去除有机物及脱氮性能的影响, 并通过高通量测序技术分析了曝气生物滤池填料生物膜的微生物群落结构特征。结果表明, 曝气量大小是影响曝气生物滤池硝化性能的直接因素, 增大曝气量有利于反应器内生物膜硝化活性的提高, 但对生物反硝化活性有抑制作用: 水力停留时间过长或过短均不利于生物膜保持高脱氮活性: 而硝化液回流增加了反应器内微生物与污染物的接触机会和反应时间, 有利于提高反应器脱氮效果。综合分析表明, 当曝气量为40 L·h-1, 水力停留时间为0.8 h时, 有硝化液回流的曝气生物滤池出水水质较好, COD平均去除率约为91.8%, NH4+-N平均去除率约为93.1%以及TN平均去除率约为50.4%。曝气生物滤池表现出良好的有机物去除效率, 并具备较高的同步硝化反硝化能力, 主要归因于填料生物膜富集了大量硝化细菌如Nitrospra和Comamonadaceae等以及反硝化细菌如Pesudomonas、Truepera和Azoarcus等。     

人工湿地黑臭水体处理系统微生物脱氮机理研究

以上海市老段浦I、II和北夏3座水平潜流人工湿地黑臭河道处理系统为研究对象,进行了水平潜流湿地处理黑臭河道氨氮的转化及脱氮机理的研究。研究表明,3座人工湿地的pH值均呈弱碱性,且沿湿地水流方向变化较小。溶解氧值在0.09—0.35mg/L范围内波动,氨氮沿湿地的流向呈递减的趋势,亚硝态氮及硝态氮浓度较低。在老段浦人工湿地的同一土样中,亚硝化细菌的数量远大于硝化细菌的数量,北夏人工湿地中,湿地前端的亚硝化细菌与硝化细菌的数量近似相等,但在湿地末端亚硝化细菌数量要远小于硝化细菌的数量。原位曝气抑制反硝化反应试验研究表明,3座人工湿地都发生了"新"的脱氮途径-短程硝化-反硝化反应,其中两座老段浦人工湿地50%的氮以短程硝化-反硝化反应去除。北夏人工湿地中约20%的氮以短程硝化反硝化的途径去除。       

亚硝化细菌的分离及初步鉴定

目的:为了使短程硝化-反硝化生物脱氮工艺能更有效地应用于含氮污废水的处理,需分离出高效的亚硝化细菌.方法:采用亚硝化细菌富集培养基选择培养和硅胶平板分离法,通过初筛、复筛,从广西大学农场菜园土中分离到一株亚硝化速率较高的菌株N4.结果:菌株N4革兰氏染色阴性,不产芽孢,细胞短杆状,呈单个排列,有一根亚极端鞭毛.结论:初步鉴定菌株N4为亚硝化单胞菌属(Nitrosomonas sp).     

我国微生物法去除氨氮研究进展

氨氮是环境污染的主要因素之一。垃圾的填埋处理导致垃圾渗滤液的产生,渗滤液中的高氨氮和高有机物让众多物理去除氨氮的方法失效。微生物去除氨氮有着快速、高效、无副产物、方便等众多优点,可以完全代替物化法。概述了微生物法去除氨氮的最新研究进展,对硝化-反硝化法、厌氧氨氧化法、异养硝化好氧反硝化、短程硝化反硝化法、同时硝化和反硝化法等方法进行了综述,并展望了生物法去除氨氮今后的研究方向,以期为氨氮去除研究提供技术支持及借鉴。     

异养硝化⁃好氧反硝化复合菌剂在垃圾渗滤液处理中的应用

垃圾渗滤液中往往含有高浓度的有机物、氨氮等污染物。异养硝化-好氧反硝化型微生物能在脱氮的同时去除部分有机物,但目前对于相关混合菌剂直接应用于垃圾渗滤液处理的研究较少。从垃圾渗滤液中筛选出6株异养硝化-好氧反硝化菌株并组配成复合菌剂F6,探究菌剂在垃圾渗滤液中的脱氮效果。分别以单一菌株和复合菌剂F6为投放原料;以不同碳氮比、活性炭浓度、转速以及微量元素浓度为影响因素,研究复合菌剂对于垃圾渗滤液中氨氮(NH{}_{\mathrm{4}}^{+}-N)、总氮(total nitrogen, TN)、化学需氧量(chemical oxygen demand, COD)的去除性能。结果表明,提高碳氮比和微量元素浓度能够促进复合菌剂F6的降解效果;当接种量为10%、碳氮比为15%时,F6对NH{}_{\mathrm{4}}^{+}-N、TN、COD的去除率分别为74.69%、89.23%和83.50%,与不添加活性炭的处理相比,分别提高了约18.46%、20.97%和7.98%。复合异养硝化-好氧反硝化菌剂F6对高氨氮垃圾渗滤液去除NH{}_{\mathrm{4}}^{+}-N、TN、COD等方面具有良好的应用前景。     

间歇曝气对微污染源水生物接触氧化修复系统脱氮性能的影响

针对寡营养生境下生物脱氮过程碳源不足等问题,开展不同间歇曝气方式对微污染源水生物接触氧化修复系统脱氮性能的影响研究,探究修复系统短程硝化反硝化的可行性与过程机理.结果表明:在停曝-曝气时间为8 h-16 h的间歇曝气方式(Ⅰ)下启动的生物接触氧化修复系统,其铵态氮(NH+4-N)、高锰酸盐指数(CODMn)、总氮(TN)的平均去除率分别稳定在93.0%、78.1%、19.4%;而在停曝-曝气时间为16 h-8 h的间歇曝气方式(Ⅱ)下运行修复系统,其NH+4-N、CODMn平均去除率仍能分别维持在81.2%、76.4%,体系内NO-2-N发生积累,TN去除率增至50%以上.对工况Ⅱ下修复系统周期内氮素转化特性分析发现,在确保出水NH+4-N、溶解氧(DO)浓度达标的前提下,缩短曝气时间可将体系DO长时间控制在0.5～1.5 mg·L-1,亚硝酸氧化菌(NOB)生长及其活性受到抑制,NO-2-N明显累积,最终实现了微污染源水生物接触氧化修复系统的短程生物脱氮.     

滇池可培养好氧反硝化细菌多样性及其脱氮特性

【目的】氮污染已成为当今水体污染的一个重要因素,为了解滇池可培养好氧反硝化细菌的多样性,获得高效好氧反硝化细菌资源,为污染水体或浅层地下水的生物修复提供材料。【方法】采用富集培养方法从滇池沉积物和水体样品中分离好氧反硝化细菌,对好氧反硝化细菌的16S r RNA基因序列进行系统发育分析,并筛选其中的高效好氧反硝化细菌。【结果】分离出260株好氧反硝化菌,经16S rRNA基因序列分析,260株菌分属于2门13科14属的59个种。假单胞菌属(Pseudomonas)为优势细菌属,其次是不动杆菌属(Acinetobacter)、气单胞菌属(Aeromonas)和代尔夫特菌属(Delftia)。筛选到12株高效好氧反硝化细菌菌株,其中8株属于假单胞菌(Pseudomonas spp.),4株为不动杆菌(Acinetobacter spp.)。定量分析发现菌株N15-6-1的反硝化效果较好。对菌株N15-6-1的脱氮条件优化结果显示,在以蔗糖为碳源,温度为30–35℃、C/N=12、静止培养时,反硝化能力较强,其在48 h内硝态氮的去除率达到98.81%,总氮的去除率达96.27%。【结论】滇池存在着较丰富的可培养好氧反硝化细菌,好氧反硝化细菌的分离丰富了好氧反硝化菌的种类,其中的高效脱氮菌株为污染水体或浅层地下水的生物修复提供了初步的候选菌株。     

垃圾填埋场N2O排放通量及测定方法研究进展

氧化亚氮(N₂O)是第三大温室气体和最主要的臭氧层破坏气体.填埋是目前城市生活垃圾处理处置的主要方式,而垃圾填埋场是N₂O的排放源之一.实验室研究和现场测定均表明,生活垃圾填埋场可以有高的N₂O释放通量,但不同填埋场测定数据差异很大.目前,对生活垃圾填埋场N₂O排放量的原位准确测定以及排放机理和重要性的认识仍有很多不足.本文概述了生活垃圾填埋场N₂O排放研究现状,从垃圾堆体和覆土层两部分探讨了传统厌氧卫生填埋场的N₂O产生和排放机理,并就此对新型脱氮型生物反应器填埋场做了相应探讨.最后,就静态箱法、涡度相关法等N₂O通量测定方法在填埋场的适用性进行了讨论,并展望了填埋场N₂O排放的研究方向.     

准好氧填埋渗滤液水质变化特性研究

在大型模拟填埋试验装置(21 m×3.8 m×6.0 m)上,研究了准好氧填埋渗滤液水质的主要指标COD_Cr、BOD、NH₃⁺-N和pH的变化特性.结果表明,准好氧填埋结构下渗滤液COD_Cr、BOD浓度下降很快,没有出现在传统填埋场累积的现象,并且封场后39周分别降为173和30 mg·L^-1;NH₃⁺-N浓度下降更为显著,第39周降为1 mg·L^-1,下降率达到99.6%,为渗滤液后续处理解决了NH₃⁺-N浓度过高的难题;pH值在前2周略低于7,第3周后一直呈弱碱性.根据实验数据,拟合了准好氧填埋结构渗滤液污染物的衰减方程.     

垃圾填埋场N_2O排放通量及测定方法研究进展

氧化亚氮(N2O)是第三大温室气体和最主要的臭氧层破坏气体.填埋是目前城市生活垃圾处理处置的主要方式,而垃圾填埋场是N2O的排放源之一.实验室研究和现场测定均表明,生活垃圾填埋场可以有高的N2O释放通量,但不同填埋场测定数据差异很大.目前,对生活垃圾填埋场N2O排放量的原位准确测定以及排放机理和重要性的认识仍有很多不足.本文概述了生活垃圾填埋场N2O排放研究现状,从垃圾堆体和覆土层两部分探讨了传统厌氧卫生填埋场的N2O产生和排放机理,并就此对新型脱氮型生物反应器填埋场做了相应探讨.最后,就静态箱法、涡度相关法等N2O通量测定方法在填埋场的适用性进行了讨论,并展望了填埋场N2O排放的研究方向.     

Effects of in situ nitrogen removal on degradation/stabilization of MSW in bioreactor landfill

The effects of in situ nitrogen removal on degradation of municipal solid waste (MSW) in bioreactor landfill system were investigated. The in situ nitrogen removal bioreactor landfill (NBL) consisted of fresh-refuse filled, methanogenic and nitrifying reactors was operated. The two-phase bioreactor landfill (BL) comprised of fresh-refuse filled and methanogenic reactors was used as control. The methanogenic and nitrifying reactors were all loaded with aged refuse whose placement time was 6-7 yr. Furthermore, the nitrifying reactor was in situ aerated. The results showed that the degradation of fresh-refuse was delayed and CH4 production also was reduced in the in situ nitrogen removal bioreactor landfill. It was feasible to perform in situ ammonia nitrification in aged refuse. Moreover, the efficiency of oxygen utility was high during the in situ nitrification because of the porous characteristic of aged refuse. Supplementing only 8.5mg O2 mg(-1)Nd(-1) to aged refuse could make ammonia removed completely. However, aeration did not accelerate the further stabilization of aged refuse.     

In situ simultaneous organics and nitrogen removal from recycled landfill leachate using an anaerobic-aerobic process

An anaerobic-aerobic process including a fresh refuse landfill reactor as denitrifying reactor, a well-decomposed refuse reactor as methanogenesis reactor and an aerobic activated sludge reactor as nitrifying reactor was operated by leachate recirculation to remove organic and nitrogen simultaneously. The results indicated that denitrification and methanogenesis were carried out successfully in the fresh refuse and well-decomposed landfill reactors, respectively, while the nitrification of NH(4)(+)-N was performed in the aerobic reactor. The maximum organic removal rate was 1.78 kg COD/m(3)d in the well-decomposed refuse landfill reactor while the NH(4)(+)-N removal rate was 0.18 kg NH(4)(+)-N/m(3)d in the aerobic reactor. The biogas from fresh refuse reactors and well-decomposed refuse landfill reactors were consisted of mainly carbon dioxide and methane, respectively. The volume fraction of N(2) increased with the increase of NO(3)(-)-N concentration and decreased with the drop of NO(3)(-)-N concentration. The denitrifying bacteria mustered mainly in middle layer and the denitrifying bacteria population had a good correlation with NO(3)(-)-N concentration.     

In situ nitrogen removal in phase-separate bioreactor landfill

The feasibility of in situ nitrogen removal in phase-separate bioreactor landfill was investigated. In the experiment, two sets of bioreactor landfill systems, namely conventional two-phase and in situ nitrogen removal bioreactor landfills, were operated. The in situ nitrogen removal bioreactor landfill (NBL) was comprised of a fresh-refuse filled reactor (NBLF), a methanogenic reactor (NBLM) and a nitrifying reactor (NBLN), while the two-phase bioreactor landfill (BL) used as control was comprised of a fresh-refuse filled reactor (BLF) and a methanogenic reactor (BLM). Furthermore, the methanogenic and nitrifying reactors used aged refuse as bulk agents. The results showed that in situ nitrogen removal was viable by phase-separation in the bioreactor landfill. In total 75.8 and 47.5 g of nitrogen were, respectively, removed from the NBL and the BL throughout the experiment. The methanogenic reactor used the aged refuse as medium was highly effective in removing organic matter from the fresh leachate. Furthermore, the aged refuse was also suitable to use as in situ nitrification medium. The degradation of fresh refuse was accelerated by denitrification in the initial stage (namely the initial hydrolyzing stage) despite being delayed by denitrification in a long-term operation.     

Characteristics of the bioreactor landfill system using an anaerobic-aerobic process for nitrogen removal

A sequential upflow anaerobic sludge blanket (UASB) and air-lift loop sludge blanket (ALSB) treatment was introduced into leachate recirculation to remove organic matter and ammonia from leachate in a lab-scale bioreactor landfill. The results showed that the sequential anaerobic-aerobic process might remove above 90% of COD and near to 100% of NH4+ -N from leachate under the optimum organic loading rate (OLR). The total COD removal efficiency was over 98% as the OLR increased to 6.8-7.7 g/l d, but the effluent COD concentration increased to 2.9-4.8 g/l in the UASB reactor, which inhibited the activity of nitrifying bacteria in the subsequent ALSB reactor. The NO3- -N concentration in recycled leachate reached 270 mg/l after treatment by the sequential anaerobic-aerobic process, but the landfill reactor could efficiently denitrify the nitrate. After 56 days operation, the leachate TN and NH4+ -N concentrations decreased to less than 200 mg/l in the bioreactor landfill system. The COD concentration was about 200 mg/l with less than 8 mg/l BOD in recycled leachate at the late stage. In addition, it was found that nitrate in recycled leachate had a negative effect on waste decomposition.     

Nitrogen transformation in the hybrid bioreactor landfill

The hybrid bioreactor landfill was promising in solid waste management. In the work, the nitrogen removal and nitrogen transformation in hybrid bioreactor landfill with sequencing of facultative anaerobic and aerobic conditions was explored. The result showed that the combination of facultative anaerobic and aerobic conditions in the hybrid bioreactor landfill was indeed effective in eliminating ammonia both from the leachate and the refuse thoroughly. About 72% of nitrogen was reduced from the landfilled fresh refuse through the operation of 357 days. At the end of the experiment, the concentrations of COD, ammonia, nitrate and TN in the leachate decreased to 399.2 mg l^?1, 20.6 mg N l^?1, 3.7 mg N l^?1 and 25.3 mg N l^?1, respectively.     

Performance and bacterial compositions of aged refuse reactors treating mature landfill leachate

Aged landfill leachates become more refractory over time and difficulty to treat. Recently, aged refuse bioreactors show great promise in treating leachates. In this study, aged refuse bioreactors were constructed to simulate landfill leachate degradation process. The characteristics of leachate were: COD_cr, ∼2200 mg/L; BOD₅, ∼280 mg/L; total nitrogen, ∼2030 mg/L; and ammonia, ∼1900 mg/L. Results showed that bioreactor could remove leachate pollutants effectively at hydraulic loading of 20 L/m³ d. The removal rate reduced when hydraulic loading doubled or temperature lowered. Effluent recirculation could alleviate the temperature effect. Combining aged refuse and slag biofilters could treat leachate more efficiently. Pyrosequencing analysis indicated that bacteria from Pseudomonas, Lysobacter, Bacillus and δ-proteobacter, Flexibacteraceae were more abundant in the samples. The Shannon index decreased at lower temperature, while evenness and equitability increased with recirculation. We suggest that filter medium and temperature may be the main factors for shaping bacterial community structure.     

Novel engineering controls to increase leachate contaminant degradation by refuse: From lab test to in situ engineering application

Here we provide direct evidence through a series laboratory and field-scale experiments using different age refuse to treat landfill leachate that aged refuse exhibits increased leachate contaminants removal ability with refuse stabilization time addition. Ten-years aged refuse showed best contaminant removal in a laboratory-scale test, removing 70.0% (8340.0-2540.0 mg/L) chemical oxygen demand (COD) and 75.0% (910.0-215.0 mg/L) ammonium-N, as well as removing 61.5-67.0% COD and 50.4-58.1% ammonium-N with variable COD (9948.0-12286.0 mg/L) and NH₃-N (780.0-1184.0 mg/L) in a field-scale test, respectively. When the 10-years aged refuse was disinfected by 20% NaClO (wt%), COD, biochemical oxygen demand (BOD₅), total nitrogen (TN), and ammonium-N removal showed a dramatic decrease throughout operation time from 84.4-86.2% to 15.2-34.5%, 94.4-99.8% to 26.2-54.4%, 31.2-33.9% to 2.1-10.1%, and 88.5-90.1% to 1.5-14.5%, respectively, suggesting biodegradation is the dominant contaminant removal. Based on this finding, a 3-stages (8 years) age refuse bioreactor (ARB) was constructed to treat leachate and ARB efficiently reduced chemical oxygen demand (COD) from 5478.0-10842.0 mg/L to 261.0-1020 mg/L (87.8-96.2% removal), ammonium-N from 811.4-1582.0 mg/L to 8.5-43.3 mg/L (96.9-99.4%), respectively, in 18 months running. In summary, the present studies suggest that increased leachate contaminant biodegradation ability of aged refuse could be used directly to create an engineering approach to treat leachate with operational and economic advantages.     

Nitrogen removal through different pathways in an aged refuse bioreactor treating mature landfill leachate

In this study, an aged refuse bioreactor was constructed to remove nitrogen in a mature landfill leachate. The nitrogen removal efficiency and the microbial community composition in the bioreactor were investigated. The results showed that the aged refuse bioreactor removed more than 90 % of total nitrogen in the leachate under the nitrogen loading rate (NLR) of 0.74 g/kg (vs) day, and the total nitrogen removal rate decreased to 62.2 % when NLR increased up to 2.03 g/kg (vs) day. Quantitative polymerase chain reaction results showed that the average cell number of ammonia-oxidizing bacteria in the bioreactor was 1.58?×?10⁸ cells/g, which accounted for 0.41 % of total bacteria. The number of anammox bacteria in the reactor was 1.09?×?10⁸ cells/g, which accounted for 0.27 % of total bacteria. Isotopic ¹⁵N tracing experiments showed that nearly 10 % of nitrogen was removed by anammox. High-throughout 454 pyrosequencing revealed that the predominant bacteria in the bioreactor were Proteobacteria, Chloroflexi, Actinobacteria, Bacteroidetes, and Gemmatimonadetes, including various nitrifiers and denitrifiers with diverse heterotrophic and autotrophic metabolic pathways, supporting that nitrogen was removed through different pathways in this aged refuse bioreactor.     

Releasing behavior of copper in recirculated bioreactor landfill

The purpose of this study was to determine the releasing behavior of copper in municipal solid waste (MSW) in landfill with respect to refuse and leachate as an inseparable system. Two simulated bioreactor landfills, one with leachate recirculation and the other without, were operated in room temperature for 320 days. Copper in refuse showed behaviors of staggered migration and retention, which corresponded with the degradation process of landfill obviously. The significant different amounts of Cu²⁺ leached out from refuse into leachate of two landfills were 24.74 mg and 118.53 mg after 320 days’ operation, respectively. It also reflected the releasing behavior of copper in landfill refuse at different stage accordingly. The results confirmed that the refuse in landfill had high potential of secondary pollution after closure.     

An innovative combined on-site process for the remote rural solid waste treatment--a pilot scale case study in China

The aim of this study was to find a feasible method for the treatment of solid waste generated in the remote rural, where the transportation costs are prohibitive and the resources to construct and maintain conventional treatment plants are not available. This process, consisted of two types of simulated bioreactor landfill (one was recirculated bioreactor landfill, and the other was comprised of fresh and aged refuse reactor) and a soil infiltration system, was operated in ambient temperature for 180 days all together. After treated by the system of fresh and aged refuse reactor, the refuse and leachate reached a strongly degraded and stable state. The remaining leachate can be treated by the soil infiltration system, and 87.5 ± 2.1%, 98.6 ± 1.0% and 95.7 ± 1.7% were achieved by 60 cm soil depths for organic matter, ammonium nitrogen and total nitrogen removal, respectively.