膜-生物硝化反应器处理含氨废水效能的研究

研究了膜 生物硝化反应器对含氨废水的处理效能以及分离膜的截留和渗透效能。膜_生物反应器启动迅速 ,在水力停留时间为 1d的情况下 ,反应器最高进水浓度达 80mmol(NH₄⁺-N)·L^-1 ,最高容积负荷达 1 12kg(NH₄⁺ -N)·m^-3·d^-1 ,氨氮去除率保持在 95%以上。试验证明 ,分离膜对微生物有良好的截留作用 ,50天内反应器的污泥浓度从 5g·L^-1 增长到 10g·L^-1 ,分离膜表面附着的生物层则对废水氨氮和亚硝氮有进一步的转化作用。在液位差低于 80cm时 ,提高液位差可增大膜渗透通量 ;液位差超过 80cm后 ,增大液位差的膜渗透通量效应很小 ;其中 ,当液位差为 2 0cm左右时 ,膜通量达 2 . 5 1L·m^-2 ·h^-1 ,阻力最小 [(2 . 6 3× 10^-5)m^-1]。该膜_生物硝化反应器可依靠液位差压力驱动出水 ,无需外加动力。     

厌氧氨氧化菌混培物生长及代谢动力学研究1

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℃。V_maxa、K_ma、K_ia和K_in的活化能依次为37.316、30.239、33.695和30473kJ·mol^-1。     

内循环颗粒污泥床硝化反应器临界曝气强度的研究

内循环颗粒污泥床硝化反应器是一种新型高效硝化反应器 ,在反应器运行过程中 ,液体循环临界曝气强度和颗粒污泥流化临界曝气强度是两个重要操作参数。建立了升流区表观液速Ulr与曝气强度Ugr之间的关系 ,并测定了有关的模型参数 ,得到了具体的数学表达式 :U_lr=(2.613-0.024 )U^0.871_gr 0.276U^0.871_gr-0.28。根据该模型 ,计算得到的液体循环临界曝气强度为1.017cm/min ,颗粒污泥流化临界曝气强度为 2.662cm/min。实测结果证明 ,求得的两个临界曝气强度具有较高的准确性 ,能够用于指导内循环颗粒污泥床硝化反应器的操作优化.     

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 anamm oxidans,Kuenenia stuttgartiensis,Scalindua sorokinii);对厌氧氨氧化     

潜流人工湿地中植物对氮磷净化影响效应的研究

采用潜流人工湿地系统,配制以NH⁺₄-N、NO^-₃-N和PO^3-₄-P为主要成分的模拟污水,通过间歇运行方式,考察了芦苇和小叶章的生长情况、生理生态学特性及其对污水中N、P净化效能的影响,并研究了植物对湿地系统pH变化、NO^-₃-N和NH⁺₄-N净化效率的影响。结果表明,当水力停留时间为7d时,小叶章和芦苇湿地对TN的去除率分别为65.1%和99.6%,去除负荷分别为1.66g · m^-3 · d^-1和2.53g · m^-3 · d^-1。小叶章和芦苇对去除TN的贡献率分别为14.7%、61.7%,对去除TP的贡献率分别为11.7%和12.9%;芦苇植株内N、P浓度分别为29.2mg/g和3.41mg/g。芦苇湿地的净化效能高于小叶章湿地。湿地系统中pH值先升高后降低的拐点可作为氨氧化反应结束的指示参数。     

硝化抑制剂对蔬菜土硝化和反硝化细菌的影响

土壤N素循环主要是微生物驱动的转化过程,然而对其的驱动与调控机理了解还很不够。选取长沙黄兴镇蔬菜基地两种蔬菜土研究硝化抑制剂(DCD)对N素转化过程及功能微生物的影响。试验通过室内土壤培养,处理为单施尿素(CK)和尿素与硝化抑制剂双氰胺配合施用(DCD),重复3次。在培养过程中系统监测了土壤中NH₄⁺-N、NO₃^--N含量变化,同时采用荧光定量PCR(real-time PCR)方法研究硝化抑制剂对土壤中氮素转化功能基因丰度的影响。结果表明:在培养过程中DCD处理使两个供试土壤的NH₄⁺浓度稳定在较高水平,而NO₃^-浓度则明显低于对照;施用DCD导致土壤中硝化基因amoA丰度显著减少,而对16S rRNA和反硝化基因nirK丰度没有产生明显影响。因此,DCD在菜地土壤中主要通过抑制氨氧化细菌的繁衍来抑制硝化作用。     

高活性反硝化颗粒污泥的研究

以上流式厌氧污泥床（ＵＡＳＢ）反应器中的反硝化颗粒污泥为样品,研究了颗粒污泥的基本特性。测定出颗粒污泥中的优势无机元素为Ｃａ、Ｐ．颗粒表面以球菌和短杆菌为主。反硝化菌是颗拉中的优势菌群,数量可达６．５ｘ１０^８－１．５ｘ１０^１０个／ｍｌ颗粒污泥。初步鉴定了两株脱氮菌Ｍｉｃｒｏｃｏｃｃｕｓｓｐ．ｓｔｒａｉｎＮ_１和ＰｓｅｕｄｏｍｏｎａｓａｅｒｕｇｉｎｏｓａｓｔｒａｉｎＮ_２．     

丛枝菌根真菌和施加不同形态氮肥对杉木幼苗养分吸收的影响

为了解丛枝菌根真菌(AMF)和不同形态氮对杉木(Cunninghamia lanceolata)生长和养分吸收的影响,以1 a生杉木幼苗接种摩西球囊霉(Glomus mosseae)和添加不同形态氮(NH₄⁺-N和NO₃^–-N),对其养分元素和生长状况的变化进行研究。结果表明,AMF显著提高了杉木的苗高和生物量,促进了杉木对N、P、K、Ca、Mg、Fe和Na的吸收,AMF对微量元素Fe、Na的促进作用总体上要强于大量元素K、Ca。与NO₃^–-N相比,AMF显著提高了NH₄⁺-N处理杉木的生物量、总C和N、Ca、Mg、Mn含量,而且这种显著性在叶中普遍高于根和茎。接种AMF可以促进杉木幼苗的生长和对养分元素的吸收,且添加NH₄⁺-N处理的促进作用要强于NO₃^–-N。     

一株耐碱变形假单胞菌ZY-3的鉴定及其脱氮特性

【背景】目前缺少具有高效脱氮能力、较高生物安全性、能处理高碱含氮污水的好氧反硝化菌株,难以使用生物方法处理高碱性的工业、养殖废水。【目的】对前期于佛山市一水产养殖池塘底泥中分离得到的耐碱高效好氧反硝化细菌ZY-3进行研究,期望获得一株能用于不同酸碱环境脱氮的高效、安全的好氧反硝化细菌。【方法】通过形态学、生理生化试验及16S rRNA基因序列分析方法对菌株种属进行鉴定,采用抗生素试验及斑马鱼攻毒试验进行菌株的环境生物安全性评估,利用3种含不同氮素的含氮模拟废水进行脱氮能力的测定。【结果】确定ZY-3为假单胞菌属变形假单胞菌（Pseudomonas plecoglossicida）,其对多种临床常用抗生素敏感,对水生生物的毒性低,该菌株在高浓度含氮模拟废水中以28℃、180 r/min振荡培养时,其对数期出现在4—12 h,在12 h时NH₄⁺-N、NO₃^--N和NO₂^--N的去除率分别达到94.87%、81.44%和98.02%,其pH耐受范围为6.0—10.0。【结论】得到一株安全、高效、具有广泛pH适应范围的耐碱好氧反硝化细菌P. plecoglossicida ZY-3,其在有氧条件下对3种氮素（NH₄⁺-N、NO₃^–-N、NO₂^–-N）具有快速去除能力。     

温度和水分变化对冻土区泥炭地土壤氮循环功能基因丰度的影响

以大兴安岭多年冻土区泥炭地为研究对象,通过室内模拟增温实验,研究温度升高对不同深度（0-150 cm）土壤氮循环功能基因丰度的影响。同时针对0-20 cm和20-40 cm土壤设置两个水分处理,分别为土壤原始含水量和淹水状态,研究水分变化对表层土壤氮循环功能基因丰度的影响。结果表明温度升高显著提高了活动层（0-60 cm）、过渡层（60-80 cm）、永冻层（80-100 cm）中nifH、nirK基因丰度,温度升高显著提高了活动层（0-40 cm）和过渡层（60-80 cm）中nirS基因丰度。温度升高显著提高了过渡层（60-80 cm）NH₄⁺-N和较深永冻层（140-150 cm）NO₃^--N的含量,但降低了过渡层（60-80 cm）NO₃^--N和较深永冻层（120-150 cm）NH₄⁺-N的含量,相关性分析表明,NH₄⁺-N含量与nifH和nirS基因丰度呈显著正相关,NO₃^--N含量与nirK基因丰度呈显著正相关,说明温度升高能够通过改变微生物丰度促进过渡层固氮作用和反硝化作用。在增温条件下,淹水处理使表层土壤nirS和nirK基因丰度及NH₄⁺-N含量降低,但提高了NO₃^--N含量,说明淹水造成了过度还原的条件使反硝化底物浓度降低,降低反硝化微生物活性进而抑制了土壤反硝化作用。该结果对于明确未来气候变化影响下冻土区泥炭地土壤氮循环过程具有重要意义。     

渗透压对硝化作用的影响

在气升式内循环硝化反应器中研究了渗透压对硝化作用的影响。保持进水氨氮浓度420mg·L-1,将进水渗透压逐渐从4.3×105Pa提高到18.8×105Pa,硝化反应器的氨氮转化率稳定在93%～100%。将进水渗透压进一步提高到19.2×105Pa,氨氮转化率降至69.2%。渗透压对硝化作用的影响具有突发性,临界值在18.8×105～19.2×105Pa之间。受高渗透压胁迫时,活性污泥中硝化细菌的形态趋向单一,个体变小,内膜数量减少,并产生许多不明成分的颗粒状内含物。解除渗透压胁迫后,细胞结构恢复。添加钾离子能够缓解高渗压对硝化作用的影响。高渗透压胁迫以及解除渗透压胁迫可增强污泥硝化活性,比污泥氨氮转化率(污泥以SS计)分别从0.083kg·kg-1·d-1升至0.509kg·kg-1·d-1和2.569kg·kg-1·d-1,同比提高5.1倍和30.0倍。     

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.     

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.     

Optimum growth requirements of nitrifying consortia developed from treated sewage

The optimum growth requirements of two nitrifying consortia developed from treated sewage by enrichment technique were determined by a series of experiments. There was total inhibition of nitrification at above 2.75 g l(-1) NH4(+)- N and 2.5 g l(-1) NO2(-)-N and the ammonia oxidizing consortium preferred a pH at 8.5 and the nitrite oxidizing consortium a pH of 7.5 as the optima for nitrification. Optimum temperatures were between 20 degrees and 30 degrees C for both the groups. As the rate of airflow was increased from 1 to 7 l/min, the build-up of NO2(-)-N increased 10-fold and the consumption of NO2(-)-N increased by a factor of 28.8 implying that the ammonia oxidizing consortium in a bioreactor required three times more aeration than that for nitrite oxidizers for expressing their full nitrifying potential. These data directly contribute for developing a fermentation process for the mass production of nitrifiers as well as for designing bioreactors for nitrifying sewage.     

Anaerobic hydrogen production with an efficient carrier-induced granular sludge bed bioreactor

A novel bioreactor containing self-flocculated anaerobic granular sludge was developed for high-performance hydrogen production from sucrose-based synthetic wastewater. The reactor achieved an optimal volumetric hydrogen production rate of approximately 7.3 L/h/L (7,150 mmol/d/L) and a maximal hydrogen yield of 3.03 mol H2/mol sucrose when it was operated at a hydraulic retention time (HRT) of 0.5 h with an influent sucrose concentration of 20 g COD/L. The gas-phase hydrogen content and substrate conversion also exceeded 40 and 90%, respectively, under optimal conditions. Packing of a small quantity of carrier matrices on the bottom of the upflow reactor significantly stimulated sludge granulation that can be accomplished within 100 h. Among the four carriers examined, spherical activated carbon was the most effective inducer for granular sludge formation. The carrier-induced granular sludge bed (CIGSB) bioreactor was started up with a low HRT of 4-8 h (corresponding to an organic loading rate of 2.5-5 g COD/h/L) and enabled stable operations at an extremely low HRT (up to 0.5 h) without washout of biomass. The granular sludge was rapidly formed in CIGSB supported with activated carbon and reached a maximal concentration of 26 g/L at HRT = 0.5 h. The ability to maintain high biomass concentration at low HRT (i.e., high organic loading rate) highlights the key factor for the remarkable hydrogen production efficiency of the CIGSB processes.     

生物反应器填埋场系统渗滤液的脱氮性能

利用填埋场垂直分布的好氧-缺氧-厌氧的独特生态环境,并采用填埋垃圾上层间歇曝气充氧的方式,研究了生物反应器填埋场系统渗滤液的脱N性能.结果表明,填埋垃圾上层间歇曝气充氧,促进了填埋垃圾层硝化细菌和反硝化细菌的生长,且可使反硝化细菌的数量比普通的填埋垃圾层高4～13个数量级,硝化细菌的最大数量可达到10⁹个·g^-1;营建了填埋场内硝化、反硝化等脱N反应的生物环境,有利于回流渗滤液含N化合物的去除.试验结束时,其渗滤液NH₄⁺-N和TN浓度分别为186和289 mg·L^-1,仅为对照的18%和26％.此外,填埋垃圾上层间歇曝气充氧也有利于填埋垃圾的降解,提高垃圾的稳定化效果.     

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.     

Organics and nitrogen removal and sludge stability in aerobic granular sludge membrane bioreactor

Novel aerobic granular sludge membrane bioreactor (GMBR) was established by combining aerobic granular sludge technology with membrane bioreactor (MBR). GMBR showed good organics removal and simultaneous nitrification and denitrification (SND) performances for synthesized wastewater. When influent total organic carbon (TOC) was 56.8-132.6 mg/L, the TOC removal of GMBR was 84.7-91.9%. When influent ammonia nitrogen was 28.1-38.4 mg/L, the ammonia nitrogen removal was 85.4-99.7%, and the total nitrogen removal was 41.7-78.4%. Moreover, batch experiments of sludge with different particle size demonstrated that: (1) flocculent sludge under aerobic condition almost have no denitrification capacity, (2) SND capacity was caused by the granular sludge, and (3) the denitrification rate and total nitrogen removal efficiency were enhanced with the increased particle size. In addition, study on the sludge morphology stability in GMBR showed that, although some granular sludge larger than 0.9 mm disaggregated at the beginning of operation, the granular sludge was able to maintain the stability of its granular morphology, and at the end of operation, the amount of granular sludge (larger than 0.18 mm) stabilized in GMBR was more than 56-62% of the total sludge concentration. The partial disaggregation of large granules is closely associated with the change of operating mode from sequencing batch reactor (SBR) system to MBR system.     

Aerobic granulation and nitrogen removal with the effluent of internal circulation reactor in start-up of a pilot-scale sequencing batch reactor

Aerobic granular sludge was successfully cultivated with the effluent of internal circulation (IC) reactor in a pilot-scale sequencing batch reactor (SBR) using activated sludge as seeding sludge. N removal was investigated in the start-up of aerobic granulation process. Initially, the phenomenon of partial nitrification was observed and nitrite accumulation rates (NO₂ ^?-N/NO _x ^? -N) were between 84.6 and 99.1?%. It was potentially caused by ammonium oxidizing bacteria (AOB) in the seeding activated sludge, high external environmental temperature (~32?°C) and free ammonia (FA) concentration. After 50?days’ running, the aerobic granules-based bioreactor demonstrated perfect performance in simultaneous removal of organic matter and ammonia nitrogen, and average removal efficiencies were maintained above 93 and 96?%, respectively. The maximum nitrogen removal efficiency of 83.1?% was achieved after the formation of aerobic granules. The average diameter of mature aerobic granular sludge mostly ranged from 0.5 to 1.0?mm. Furthermore, one typical cyclic test indicated that pH and DO profiles could be used as effective parameters for biological reactions occurring in the aerobic/anoxic process. The obtained results could provide further information on the cultivation of aerobic granular sludge with practical wastewater, especially with regard to nitrogen-rich industrial wastewater.