苯甲酸对反硝化细菌氮素转化的影响机制

选取苯甲酸为研究对象,探究不同浓度的苯甲酸对铜绿假单胞菌及脱氮副球菌反硝化过程的影响。外源添加不同浓度的苯甲酸于细菌培养液中并厌氧培养,动态监测其细菌生长情况pH、反硝化氮素产物、最终苯甲酸含量及相关反硝化酶活性。结果表明：(1)苯甲酸为1、2 mmol/L时,铜绿假单胞菌N₂O产生量分别增加了62.3%和28.4%,3、4 mmol/L时降低了29.7%和92.6%;不同浓度苯甲酸均可抑制脱氮副球菌N₂O产生,抑制率为19.3%～99.8%;(2)苯甲酸对铜绿假单胞菌的生长是低浓度促进、高浓度抑制,高浓度苯甲酸对其反硝化的限速步骤在NO^-₃的还原;(3)各浓度苯甲酸对脱氮副球菌的生长均呈抑制作用,苯甲酸对脱氮副球菌的NO^-₃还原影响较小,高浓度苯甲酸可抑制NO^-₂还原过程。因此,铜绿假单胞菌和脱氮副球菌的反硝化过程对苯甲酸浓度的响应存在明显差别。研究揭示了不同特性反硝化细菌对苯甲酸浓度响应差异性机制,为深入理解...     

好氧反硝化菌TAD1的同步硝化反硝化性能

研究发现嗜热螯台球菌(Chelatococcus daeguensis)TAD1具有同步硝化反硝化性能,可将水中的氨氮去除。重点考察50℃下,碳氮比、碳源、初始pH值、DO浓度等因素对菌株TAD1同步硝化反硝化脱氮性能的影响规律及菌株TAD1的耐氨能力,最后用Minitab软件进行综合优化。结果表明,菌株TAD1在高浓度氨氮(500～3 000 mg/L)下仍具有很高的脱氮能力,pH值和碳源用量是影响TAD1同步硝化反硝化最显著的因素,综合优化后总氮最大去除率达到了70%,证实利用菌株TAD1的同步硝化反硝化性能具有潜在的废水脱氮应用前景。     

一体化A/O生物膜反应器脱氮特性研究

采用新型的一体化A/O生物膜反应器,对生活污水进行脱氮处理实验.研究了溶解氧(DO)质量浓度对硝化和反硝化作用的影响,并对反应器的脱氮特性和降解机理进行了探讨.结果表明:DO对一体化A/O反应器脱氮影响较大,随着好氧区DO的增加,NH3-N和TN的去除率相应增加.当DO为2～4 mg/L时,发生同步硝化反硝化作用,NH...     

纳米铁系双金属-微生物体系去除地下水NO-3-N研究

采用不同液相还原法制备纳米Fe0、Fe/Ni和Fe/Cu粒子,将其与反硝化细菌混合应用于地下水NO3--N去除研究。考察3种体系对NO3--N去除速率的影响,并对其脱氮产物及RNA水平上纳米铁系双金属对反硝化细菌的毒性效应进行了分析和讨论。结果表明,9 d内纳米Fe0体系可完全将NO3--N去除,过程中伴随NO2--N先升高后降低的生成趋势,NH 4+-N生成52%;纳米Fe/Ni体系脱氮速率最快,6 d内可将NO 3--N完全去除,几乎未检测到NO 2--N的生成,而NH 4+-N的转化率高达69%;纳米Fe/Cu体系7 d内可将NO3--N去除完全,NH4+-N的生成率降低,仅39%,但是出现33%NO2--N积累。从反应前后反硝化细菌总RNA浓度变化看,3种纳米粒子对反硝化细菌的毒性大小为纳米Fe/Ni﹥纳米Fe/Cu﹥纳米Fe0。     

一株耐盐好氧反硝化细菌的分离鉴定及其脱氮特性

从处理高盐废水的生物接触氧化工艺成熟活性污泥中分离得到一株耐盐好氧反硝化细菌F10.根据形态学特征、生理生化以及16S rRNA基因序列测定分析,初步判定该菌株为盐单胞菌属(Halomonas sp.).菌株能在盐度为3%~7%的培养基中良好的生长及脱氮,最适盐度为3%(以Na Cl计),最适碳源为乙酸钠,最适p H为7~8,最适温度为30℃.该菌株能利用NO-3-N进行反硝化作用,在盐度为3%的反硝化培养基中24 h内对NO-3-N的去除率达到92.6%,36 h基本完全去除。该菌株在3%盐度下表现出良好的异养硝化-好氧反硝化性能,初始硝态氮浓度在270 mg/L时,菌株的脱氮率可达90%以上,氨氮的去除率可达75%以上,脱氮过程中无NO-2-N积累,可实现同步硝化反硝化,具有一定的工程应用价值。     

一株深海反硝化菌的分离鉴定及反硝化特性研究

从深海沉积物中分离获得一株具有较高脱氮效率的反硝化菌YL-1,通过形态观察、生理生化特性及16SrDNA同源性分析,确定该菌株为蒙氏假单胞菌(Pseudomonas monteilii)。考察了C、N质量比(C/N)、碳源、初始pH、温度及盐度对其反硝化作用的影响。结果表明:菌株YL-1反硝化最佳条件为最适碳源为乙酸钠、C/N不低于6∶1、初始pH为7.0~9.0、温度为25~35℃;该菌株具有较强的反硝化性能,盐度在100g/L以内时对其反硝化特性影响不大。     

不同分子量聚乳酸的异养反硝化脱氮性能及脱氮反应机制

聚乳酸(PLA)是一种发展潜力巨大的反硝化固体碳源。为探究不同分子量PLA反硝化脱氮路径及机制,以不同分子量PLA为固体碳源研究了PLA的静态释碳性能和反硝化脱氮效果,考察了反硝化出水溶解性有机质(DOM)组分和微生物群落结构。结果表明：PLA释碳稳定,在清水和脱氮反应器中出水COD均能稳定在20 mg·L^-1;PLA分子量越低,脱氮效果越好,5 000 g·mol^-1分子量PLA的NO₃^--N去除率和反硝化速率达到100%和1.29 mg·L^-1·h^-1。PLA脱氮路径有2条：一是反硝化功能菌群利用水解微生物分解PLA释放的小分子碳源作为电子供体进行异养反硝化作用;一是微生物利用溶解性微生物代谢产物等有机物进行反硝化脱氮。该研究结果可为PLA固体碳源在反硝化脱氮工艺中的高效应用提供参考。     

贫营养好氧反硝化菌群的筛选及源水脱氮特性

为了对低浓度氮污染的水体进行净化,通过对微污染水库沉积物进行富集驯化培养,得到好氧反硝化脱氮混合菌。对混合菌进行传代培养得到10~#为效果最好的混合菌。将10#混合菌投加到微污染水库源水中进行投菌实验。实验结果表明:投菌系统的硝氮从初始的(0.38±0.03)mg/L降到(0.07±0.03)mg/L,硝氮的去除率达到(82.30±2.63)%,而空白对照系统的硝氮从初始的(0.34±0.00)mg/L到30 d实验结束变为(0.69±0.01)mg/L;复合菌投菌系统并没有出现亚硝氮的积累;投菌系统总氮从初始的(1.00±0.04)mg/L,到30 d实验结束时总氮下降到(0.52±0.03)mg/L,去除率达到(48.24±2.82)%,但是空白对照系统的总氮从初始的(1.13±0.06)mg/L到30 d结束时为(1.17±0.03)mg/L,基本保持稳定;复合菌系统的好氧反硝化菌菌落数高于空白系统1~2两个数量级。脱氮效果表明,应用复合好氧反硝化菌对于源水脱氮有很好的应用潜力。     

一株反硝化细菌的分离鉴定及其反硝化特性

从处理城镇污水的移动床生物膜反应器中分离获得一株反硝化细菌D3,并进一步研究该菌株的系统发育地位及反硝化特性。采用16S rDNA序列分析对菌株进行初步鉴定,探讨了基质浓度、起始pH和温度对菌株反硝化活性的影响。根据形态学特征、生理生化特性及16S rDNA序列测定分析,初步鉴定菌株属于寡养单胞菌属。该菌能利用硝酸钠或亚硝酸钠进行反硝化作用,最佳电子受体是硝酸盐氮,反硝化速率最大为19.86 mg/(L·h),最适生长pH为7.36,最适生长温度为33.5℃。菌株D3在初始硝态氮浓度为140 mg/L,以乙酸钠为惟一碳源,pH为7.36,温度33.5℃的最优生长条件下,培养10 h进入对数生长期,倍增时间为9.9 h,48 h内硝酸盐还原率达95%。     

MFC强化同步短程硝化反硝化工艺的启动

微生物燃料电池(MFC)可在阴极实现反硝化、短程反硝化和同步硝化反硝化并产生电能,但在MFC阴极实现同步短程硝化反硝化的研究尚未见到报道。为了探讨MFC阴极同步短程硝化反硝化工艺的性能,将双室曝气阴极MFC与A/O脱氮工艺结合处理人工模拟低碳氮比废水。通过静置运行15 d使得MFC阴极室亚硝态氮得以积累,氨氧化菌得以富集。随即改为连续运行后第21天成功启动同步短程硝化反硝化MFC;阴极出水氨氮浓度为0.3 mg/L,亚硝态氮浓度为15.9 mg/L,硝态氮浓度为0.6 mg/L,亚硝化率达到95%以上,阴极电极自养反硝化去除率达到50%以上,COD去除率达到85%以上。结果表明,将MFC与同步短程硝化反硝化工艺结合,通过阴极室中氧气得电子获得高p H,可以强化同步短程硝化反硝化工艺,完成生物脱氮的同时回收电能,并具有减少外加碱度的优势。     

Alcaligenes sp.YF11菌对杀灭菊酯的降解机理

测定了降解菌Alcaligenessp.YF11对不同浓度杀灭菊酯的降解及其降解途径。在纯培养系统中,Alcaligenessp.YF11对100mg／L的杀灭菊酯的降解符合零级动力学特征,其降解速率为2．1mg／L·h;50mg／L的杀灭菊酯在24h的降解率为87.5％;10mg／L的杀灭菊酯10h的降解率为71．0％。Alcaligenesso．YF11对杀灭菊酯的降解为矿化作用。     

Effect of reactive media composition and co-contaminants on sulfur-based autotrophic denitrification

As a part of a study developing a biological reactive barrier system to treat nitrate-contaminated groundwater, the effects of reactive media composition and co-contaminants on sulfur-oxidizing autotrophic denitrification were investigated. The size of sulfur granules affected the denitrification rates; kinetic constants of 2.883, 2.949, and 0.677 mg-N(1/2)/L(1/2)/day were obtained when the granule sizes were below 2 mm, between 2 and 5 mm, and over 5 mm, respectively. When the volume ratios of sulfur to limestone were 1:1, 2:1, 3:1, and 4:1, kinetic constants of 5.490, 3.903, 4.072, and 2.984 mg-N(1/2)/L(1/2)/day were obtained, respectively. The presence of TCE up to 20 mg/L didn't significantly affect nitrate removal efficiency. At the TCE concentration of 80 mg/L, however, nitrate removal was markedly inhibited. Also, Zn and Cu inhibited the denitrification activity at more than 0.5 mg/L of concentration whereas Cr (VI) did not significantly affect the nitrate removal efficiency at all levels tested.     

脱氮副球菌YF1微生物燃料电池生物阴极脱氮和产电

以脱氮副球菌YF1构建纯种生物阴极微生物燃料电池(microbial fuel cell,MFC)进行脱氮和产电机理的研究。研究结果发现,阴极碳氮比、pH值对产电和脱氮效率有明显影响。当MFC的阴极运行条件pH值为8.0,碳氮比为20时,运行时间15 h时,脱氮率高达100%,输出电压为150 mV。上述结果表明,微生物燃料电池运行过程中,细菌降解硝酸根的机理为将硝酸根还原为N2或者直接将其作为自身的营养物质而利用。循环伏安(CV)与扫描电镜(SEM)的结果表明,在微生物燃料电池运行中,副球菌YF1通过接触导电作为产电的电子供体。     

矿物载体锯末碳源低温生物修复硝酸盐污染地下水

研究了低温条件下,沸石和火山岩为载体,锯末为碳源的生物反应器对地下水中硝酸盐氮的去除效果。结果表明,在（14±1）℃,水力停留时间18 h,进水硝酸盐氮浓度为27 mg/L的条件下,以锯末为碳源能有效去除地下水中的硝酸盐,沸石为载体时对硝酸盐氮的平均去除率为98%;火山岩为载体时对硝酸盐氮的平均去除率为95%。实验过程中出现铵盐和亚硝酸盐的积累,出水中氨氮浓度为1～2.55 mg/L,亚硝酸氮浓度为0～0.98 mg/L。出水pH均介于7～8,满足饮用水标准中pH的要求（6.5～8.5）。     

Removal of added nitrate in the single, binary, and ternary systems of cotton burr compost, zerovalent iron, and sediment: Implications for groundwater nitrate remediation using permeable reactive barriers

Recent research has shown that carbonaceous solid materials and zerovalent iron (Fe(0)) may potentially be used as media in permeable reactive barriers (PRBs) to degrade groundwater nitrate via heterotrophic denitrification in the solid carbon system, and via abiotic reduction and autotrophic denitrification in the Fe(0) system. Questions arise as whether the more expensive Fe(0) is more effective than the less expensive carbonaceous solid materials for groundwater nitrate remediation, and whether there is any synergistic effect of mixing the two different types of materials. We carried out batch tests to study the nature and rates of removal of added nitrate in the suspensions of single, binary, and ternary systems of cotton burr compost, Peerless Fe(0), and a sediment low in organic carbon. Cotton burr compost acted as both organic carbon source and supporting material for the growth of indigenous denitrifiers. Batch tests showed that cotton burr compost alone removed added nitrate at a greater rate than did Peerless Fe(0) alone on an equal mass basis with a pseudo-first-order rate constant k=0.0830+/-0.0031 h(-1) for cotton burr compost and a k=0.00223+/-0.00022 h(-1) for Peerless Fe(0); cotton burr compost also removed added nitrate at a faster rate than did cotton burr compost mixed with Peerless Fe(0) and/or the sediment. Furthermore, there was no substantial accumulation of ammonium ions in the cotton burr compost system, in contrast to the systems containing Peerless Fe(0) in which ammonium ions persisted as major products of nitrate reduction. It is concluded that cotton burr compost alone may be used as an excellent denitrification medium in a PRB for groundwater nitrate removal. Further study is needed to evaluate performance of its field applications.     

A2/O工艺缺氧池中反硝化聚磷菌的比例、特性研究及菌株鉴定

用释磷/聚磷装置和微生物筛选、分离方法研究A2/O工艺缺氧池污泥,确定缺氧池中反硝化聚磷菌(DPB)的比例,筛选、分离得反硝化聚磷单菌株且对单菌株聚磷特性进行研究.结果表明,缺氧池中DPB占聚磷菌(PAO)的比例约为21.5%.从缺氧池分离得到的肠杆菌科、气单胞菌属和假单胞菌属都是DPB,而不动杆菌属仅是好氧PAO,葡萄球菌属和微球菌属仅是一种专职的反硝化菌.反应过程中同时存在O2和NO3时,肠杆菌科优先利用水中的O2进行聚磷;在缺氧环境中,肠杆菌科在COD为30mg/L时的聚磷效果优于COD为180 mg/L时的聚磷效果.可见DPB的反硝化和聚磷的特性与电子受体的存在形式和COD有密切关系.因此,改良传统A2/O工艺和研发同步反硝化聚磷装置时,必须控制缺氧反硝化聚磷单元中混合液的DO和COD.     

Inhibition of sulfide generation in a reclaimed wastewater pipe by nitrate dosage and denitrification kinetics.

Sulfide generation should be avoided during wastewater transportation. The efficiency of nitrate dosing for the inhibition of sulfide generation was evaluated during reclaimed wastewater transport with two nitrate doses, 2.5 and 5 mg/L nitrate-nitrogen (NO3-N). A calcium nitrate [Ca(NO3)2] solution was injected at the beginning of the 61-km-long gravity pipe, which is part of the Reclaimed Wastewater Reuse System of South Tenerife (Spain). During transportation, after dissolved oxygen depletion, a denitrification process took place. With the 5 mg/L NO3-N dose, nitrate was not completely removed at the end of the pipe, whereas with 2.5 mg/L NO3-N, a complete denitrification was achieved. Sulfide generation was completely inhibited with the 5 mg/L dose. However, with 2.5 mg/L, sulfide generation was not completely inhibited but delayed and minimized to a great extent. Denitrification was stoichiometrically limited by the availability in biodegradable matter. An empirical equation enables one to predict the nitrate concentration.     

Kinetics of reductive denitrification by nanoscale zero-valent iron

Zero-valent iron powder (Fe0) has been determined to be potentially useful for the removal of nitrate in the water environment. This research is aimed at subjecting the kinetics of denitrification by nanoscale Fe0 to an analysis of factors affecting the chemical denitrification of nitrate. Nanoscale iron particles with a diameter in the range of 1-100 nm, which are characterized by the large BET specific surface area to mass ratio (31.4 m2/g), removed mostly 50, 100, 200, and 400 mg/l of nitrate within a period of 30 min with little intermediates. Compared with microscale (75-150 microm) Fe0, end product is not ammonia but N2 gas. Kinetics analysis from batch studies revealed that the denitrification reaction with nanoscale Fe0 appeared to be a pseudo first-order with respect to substrate and the observed reaction rate constant (k(obs)) varied with iron content at a relatively low degree of application. The effects of mixing intensity (rpm) on the denitrification rate suggest that the denitrification appears to be coupled with oxidative dissolution of iron through a largely mass transport-limited surface reaction (<40 rpm).     

高岭土负载纳米铁镍双金属去除水中偶氮染料直接耐晒黑G

采用液相还原法制备焙烧高岭土负载纳米铁镍双金属（CK-Fe/Ni）。考察了在不同条件下,如pH、投加量、初始浓度、温度等,对负载型纳米铁镍双金属降解水中偶氮染料直接耐晒黑G的影响及动力学研究。结果表明：在pH=9.49、温度为30℃、负载型纳米铁镍双金属的投加量为1.05 g/L、搅拌速度为60 r/min,经过20 min反应后,负载型纳米铁镍双金属降解水中偶氮染料直接耐晒黑G的去除率达到了99.98%。吸附和电镜表征结果表明,作为载体的焙烧高岭土起着吸附直接耐晒黑G和分散纳米铁镍双金属颗粒的作用导致反应活性提高。降解动力学数据表明,负载型纳米铁镍双金属对直接耐晒黑G的降解过程符合伪一级反应动力学规律,速率常数k随负载型纳米铁镍双金属的投加量的增加而提高,表观活化能为19.72 kJ/mol。最后,利用高岭土负载纳米铁镍双金属对废水处理,结果表明,负载型纳米铁镍双金属在实际废水中对直接耐晒黑G的去除率达到了99.98%。