长茎葡萄蕨藻在模拟工厂化循环水养殖环境中的脱氮研究

为优化工厂化循环水养殖尾水处理效果, 探究长茎葡萄蕨藻在工厂化循环水养殖条件下对含氮污染物的去除效果。采用模拟养殖尾水, 考察了长茎葡萄蕨藻对氨氮、亚硝酸盐氮、硝酸盐氮的吸收效果, 进而讨论了不同水力停留时间对长茎葡萄蕨藻吸收去除三氮的影响。结果表明, 长茎葡萄蕨藻在单一含氮污染物中硝酸盐氮吸收速率最快; 在混合含氮污染物中, 氨氮吸收速率最快, 吸收去除效率最高, 其次为硝酸盐氮。长茎葡萄蕨藻在实验条件下养殖密度为16 g·L-1时生长较快, 氨氮、亚硝酸盐氮和硝酸盐氮的去除率为92.63%、61.91%和66.08%。在水流动状态下, 水力停留时间越短, 对三氮的综合去除效果较好, 水力停留时间为4 h时氨氮、亚硝酸盐氮、硝酸盐氮去除率为55.79%、56.37%、58.50%。     

高硝化活性亚硝酸盐氧化细菌的培养和应用研究

针对本实验室筛选得到的一株亚硝酸盐氧化细菌(nitrite-oxidizingbacteria),研究了在28℃~30℃、摇床转速为110r/min时,pH、氮源、碳源、NaCl、有机物对菌体生长的影响。结果表明,培养基pH8·0~8·5、NaNO2含量4,500mg/L、Na2CO3含量1·5g/L、NaCl含量0~0·5%、葡萄糖含量0~0·1%时,亚硝酸盐氧化细菌生长良好,培养9d时,细菌浓度可达4·6×109MPN/mL,且培养基中的NO2--N能全部被硝化为NO3--N。培养基中NaCl含量大于0·5%、葡萄糖含量大于0·1%时,亚硝酸盐氧化细菌对氮源的利用受到抑制。亚硝酸盐氧化细菌降解淡水养殖池塘中的NO2--N试验表明,在水温25℃、pH8·6的池塘中,NO2--N从菌体投放后的第3d开始下降,18d后NO2--N由1·47mol/L下降至0·49mol/L。     

高硝性化活亚硝酸盐氧化细菌的培养和应用研究

针对本实验室筛选得到的一株亚硝酸盐氧化细菌(nitrite-oxidizingbacteria),研究了在28℃~30℃、摇床转速为110r/min时,pH、氮源、碳源、NaCl、有机物对菌体生长的影响。结果表明,培养基pH8·0~8·5、NaNO2含量4,500mg/L、Na2CO3含量1·5g/L、NaCl含量0~0·5%、葡萄糖含量0~0·1%时,亚硝酸盐氧化细菌生长良好,培养9d时,细菌浓度可达4·6×109MPN/mL,且培养基中的NO2--N能全部被硝化为NO3--N。培养基中NaCl含量大于0·5%、葡萄糖含量大于0·1%时,亚硝酸盐氧化细菌对氮源的利用受到抑制。亚硝酸盐氧化细菌降解淡水养殖池塘中的NO2--N试验表明,在水温25℃、pH8·6的池塘中,NO2--N从菌体投放后的第3d开始下降,18d后NO2--N由1·47mol/L下降至0·49mol/L。     

潜流-上行垂直流复合人工湿地对氮磷去除效果

研究了潜流-上行垂直流复合人工湿地工艺对NH4+-N、NO3--N、TN和TP的去除效果。在处理负荷为30 L.d-1,水力停留时间为4.8 d时,该工艺对NH4+-N、NO3--N、TN和TP具有良好的去除效果,平均去除率分别为95%、52%、79%和81%。对3种含氮化合物的去除效果可以根据运行时间分为两阶段,在两阶段中,对NH4+-N、NO3--N和TN的平均去除率分别为93%和99%,35%和98%,71%和98%。对TP的去除效果在整个试验过程中则保持稳定。     

Pseudomonas alcaliphila AD-28的脱氮性能及其关键酶活性

【背景】异养硝化-好氧反硝化菌由于能够同时实现硝化反硝化作用而备受关注,但由于菌的种类不同,其脱氮途径不尽相同,研究菌株脱氮关键酶的种类及其活性可以推测菌株的脱氮途径,从而为菌株在生产上的应用提供技术支撑。【目的】研究Pseudomonas alcaliphila AD-28的脱氮性能及其关键酶的活性,为菌株脱氮分子机理研究奠定基础。【方法】以柠檬酸钠为碳源,以硫酸铵、亚硝酸钠、硝酸钾为氮源,研究菌株AD-28的脱氮性能并检测其关键酶氨单加氧酶(AMO)、羟胺氧化还原酶(HAO)、亚硝酸盐还原酶(NIR)、硝酸盐还原酶(NAR)的酶活性。【结果】菌株AD-28培养24h的菌密度(OD600)可达1.971,对初始浓度为18.85mg/L的氨氮、26.13mg/L的硝酸盐氮、19.47mg/L的亚硝酸盐氮、66.11 mg/L的总氮去除率均达到96%以上;关键酶AMO、HAO、NIR和NAR的比活力分别为0.028、0.003、0.011、0.027 U/mg。【结论】Pseudomonas alcaliphila AD-28能同时进行异养硝化-好养反硝化作用,该菌在AMO作用下将NH4+-N氧化为羟胺,然后由HAO氧化为NO2--N,NO2--N和NO3--N在NIR、NAR等酶的催化作用下脱氮。     

一株养殖水体中亚硝酸盐去除菌的鉴定及其去除条件

【目的】从养殖污泥中分离筛选优良亚硝酸盐去除菌,并对其去除条件进行研究。【方法】从养殖污泥中分离亚硝酸盐去除菌,进一步通过测定比较分离菌株对亚硝酸盐的去除率,筛选优良的亚硝酸盐去除菌,通过API ID32GN细菌鉴定系统以及16S rDNA序列分析法对其进行鉴定,并采用单因子法研究其去除亚硝酸盐的条件。【结果】从养殖污泥中分离筛选了一株优良的亚硝酸盐去除菌AQ-3,其对50 mg/L亚硝酸盐的去除率高达99.47%。菌株AQ-3被鉴定为鲍曼氏不动杆菌(Acinetobacter baumannii)(GenBank登录号:JF751054.1),其16S rDNA序列与基因库中不动杆菌属菌株的16S rDNA序列有99%?100%的同源性,而且与鲍曼氏不动杆菌KF714株(GenBank登录号:AB109775)的亲缘关系最近。菌株AQ-3去除亚硝酸盐的最适初始pH范围为7?9,最佳碳源为乙酸钠和丁二酸钠,而且随着初始菌浓度的不断增大,菌株AQ-3对亚硝酸盐的去除率显著升高;随着亚硝酸盐浓度的不断增大,菌株AQ-3对亚硝酸盐的去除率逐渐降低。【结论】在丰富亚硝酸盐去除菌种质资源的同时,为该菌在养殖水体中的实际应用提供了理论基础。     

反硝化除磷菌筛选及其特性研究

【目的】研究反硝化除磷菌特性。【方法】通过微生物筛选和生物学特性研究方法,从对虾养殖池塘中筛选出多株可在有氧条件下同时具有反硝化除磷功能的菌种。【结果】菌株LY-1可在18 h内将初始量为10 mg/L的亚硝酸盐氮降低至0.04 mg/L,PO43?-P降低至0.05 mg/L。在DO浓度为5.0?5.9 mg/L时,该菌反硝化除磷率近100%。试验选取具有反硝化除磷功能的枯草芽孢杆菌为阳性对照菌,大肠杆菌为阴性对照菌,比较研究了菌株LY-1在不同pH、温度、盐度、PO43?-P浓度、亚硝酸盐浓度时反硝化除磷的强弱,在pH为5?9范围时,该菌亚硝酸盐氮去除率近99%,PO43?-P去除率86%;温度为30°C时,该菌反硝化除磷率近100%;盐度为5‰?15‰、PO43?-P浓度为10 mg/L、亚硝酸盐氮浓度为20 mg/L时,该菌亚硝酸盐氮和PO43?-P去除率均可达99%。【结论】菌株LY-1反硝化除磷性能显著高于对照菌(P<0.05)。通过菌株LY-1形态学观察、生理生化及16S rRNA基因序列分析,初步鉴定为蜡样芽孢杆菌(Bacillus cereus)。     

固定化微生物处理模拟污染地表水

以聚乙烯醇和海藻酸钠为包埋剂、驯化后的活性污泥为包埋菌剂,制备固定化微生物颗粒,其中包埋剂与包埋菌剂的比例为2:1。将该固定化微生物颗粒按20%的填充率装填到自制反应器中,用于处理模拟污染地表水,研究该固定化微生物的性能特点及其对模拟污染地表水的净化效果。结果表明:固定化微生物反应器的最佳水力停留时间为10h,最佳进水COD负荷为1.15～1.85g·L-1·d-1。在水温为20～29℃、溶解氧为3～4mg·L-1、水力停留时间为10h的条件下,当进水COD浓度为70.58～91.76mg·L-1、铵氮浓度为13.68～17.82mg·L-1时,COD去除率>62.3%,铵氮去除率>90.6%,表明固定化微生物能够有效地去除污染地表水中的COD和铵氮。     

一株海水异养硝化-好氧反硝化菌系统发育及脱氮特性

【目的】确定一株分离自海水的异养硝化-好氧反硝化菌的系统发育地位并探索其脱氮特性和机理,以期为解释异养硝化-好氧反硝化机理以及改进海水养殖及废水的生物脱氮工艺提供理论依据。【方法】通过形态观察、生理生化实验和16S rRNA基因序列分析,鉴定该菌株;通过测定菌株在不同无机氮源降解测试液中的生长和脱氮效率,分析其异养硝化和好氧反硝化性能。【结果】经鉴定该菌株属于盐单胞菌属(Halomonas);最适生长条件为盐度3%、pH 8.5、温度28℃、碳氮比10:1,在盐度为15%的培养液中仍能生长;可以同时去除氨氮、亚硝酸氮和硝酸氮,24 h时对NH4+-N、NO2--N、和NO3--N的去除率可分别达到98.29%、99.07%、96.48%,3种形态无机氮同时存在时,会优先利用NH4+-N,且总无机氮去除率较单一存在时更高,说明该菌株可实现同步硝化反硝化。【结论】该分离自海水的异养硝化-好氧反硝化菌属于盐单胞菌属(Halomonas),在高盐环境中仍能生长,同时具有高效的异养硝化和好氧反硝化能力,能够独立完成脱氮的全部过程。     

耐冷好氧亚硝酸盐型反硝化细菌的鉴定及脱氮特性研究

旨在对获得的具有耐冷高效去除亚硝酸盐氮和总氮的好氧反硝化细菌进行分类地位及除氮特性研究。结合形态学观察、特异性磷脂脂肪酸检测和16S r RNA基因序列分析,对实验室新分离获得的Y-9菌株进行鉴定,在此基础上,研究了温度、转速、p H、接种量、碳源和亚硝酸盐氮浓度等不同条件对该菌脱氮能力的影响。结果显示,菌株Y-9属于恶臭假单胞菌(Pseudomonas putida),还原亚硝酸盐氮的最适温度为15℃,最佳溶解氧水平对应转速为100 r/min,在该溶解氧水平下15℃、48 h内对亚硝酸盐氮和总氮的去除率高达100%和77.13%,最佳p H为7,100 m L反硝化培养基中最适接种量为1 m L OD600为0.5的菌悬液,碳源为柠檬酸钠,适合治理低浓度的亚硝酸盐氮污染水体,但对高浓度的亚硝酸盐氮具有一定耐受性。Y-9为一株耐冷反硝化细菌,在亚硝酸盐污染的养殖水体,尤其是冷水鱼类养殖水体中具有较大的应用潜力。     

固定化微生物菌剂与蕹菜对中华鳖养殖污水的净化效果研究

为解决中华鳖(Trionyx sinensis)养殖所造成的水环境污染问题,研究利用海藻酸钠、沸石对复合光合菌剂和枯草芽孢杆菌菌剂分别进行固定化,并研究了不同固定化微生物菌剂与蕹菜对中华鳖养殖污水的净化效果。结果表明:净化处理15d后,利用固定化微生物菌剂与蕹菜共同处理组对中华鳖养殖污水的净化处理效果最好,养殖污水的CODMn、NH 4+-N、NO3-N、NO 2-N、PO34的去除率分别为88.7%、87.3%、90.8%、98.3%、74.9%。蕹菜处理组对于NO3-N、NO 2-N、NH 4+-N的去除率显著高于固定化复合光合菌剂处理组和固定化枯草芽孢杆菌处理组。固定化复合光合菌剂处理组对于NO3-N、NO 2-N、NH 4+-N的去除率显著高于固定化枯草芽孢杆菌菌剂处理组,但固定化枯草芽孢杆菌处理组对于污水的CODMn的去除率最高,可达90.6%。     

Glyphosate degradation by immobilized bacteria: laboratory studies showing feasibility for glyphosate removal from waste water.

To evaluate immobilized bacteria technology for the removal of low levels of glyphosate (N-phosphonomethylglycine) from aqueous industrial effluents, microorganisms with glyphosate-degrading activity obtained from a fill and draw enrichment reactor inoculated with activated sludge were first exposed to glyphosate production wastes containing 500-2000 mg glyphosate/L. The microorganisms were then immobilized by adsorption onto a diatomaceous earth biocarrier contained in upflow Plexiglas columns. The columns were aerated, maintained at pH 7.0-8.0, incubated at 25 degrees C, supplemented with NH4NO3 (50 mg/L), and exposed to glyphosate process wastes pumped upflow through the biocarrier. Glyphosate degradation to aminomethylphosphonic acid was initially > 96% for 21 days of operation at flows yielding hydraulic residence times (HRTs) as short as 42 min. Higher flow rate studies showed > 98% removal of 50 mg glyphosate/L from the waste stream could be achieved at a HRT of 23 min. Glyphosate removal of > 99% at a 37-min HRT was achieved under similar conditions with a column inoculated with a pure culture of Pseudomonas sp. strain LBr, a bacterium known to have high glyphosate-degrading activity. After acid shocking (pH 2.8 for 18 h) of a column of immobilized bacteria, glyphosate-degrading activity was regained within 4 days without reinoculation. Although microbial growth and glyphosate degradation were not maintained under low organic nutrient conditions in the laboratory, the low levels of degradable carbon (45-94 mg/L) in the industrial effluent were sufficient to support prolonged glyphosate-degrading activity. The results demonstrated that immobilized bacteria technology is effective in removing low levels of glyphosate in high-volume liquid waste streams.     

Purification of nitrate-rich agricultural runoff by a hydroponic system

The purification of nitrate-rich agricultural runoff by a floating-raft (FR) hydroponic system was investigated at 3-, 2- and 1-d hydraulic retention times (HRTs) with particular emphasis on nitrogen conversion and removal through the system. The FR system has a dissolved oxygen (DO) environment similar to the horizontal subsurface flow system, generally 0.00mgL(-1), that facilitates denitrification. An efficient nitrate-nitrite-nitrogen (NO(x)-N) removal, 91%, 97% and 71% on average at 3-, 2- and 1-d HRT, respectively, was frequently achieved. The mean retentions were 17-47% for chemical oxygen demand, 31-64% for total nitrogen, and 8-15% for total phosphorus for the FR system. Mass balance analysis implied that the detectable DO concentration in the reactor, as low as 0.7mgL(-1), played a very important role in the conversion and removal of NH(3)-N and NO(x)-N, which finally affected the NO(x)-N removal at 3-d HRT.     

Biological denitrification using cross-linked starch/PCL blends as solid carbon source and biofilm carrier

A novel kind of cross-linked starch/polycaprolactone (SPCL11) was prepared and used as carbon source and biofilm attachment carrier for denitrifying bacteria. The results showed that the average denitrification rate was 0.027 mg NO?-N/(g·h) in batch tests. The continuous fixed-bed experiments indicated that more than 90% NO?-N was removed, the denitrification rate reached 26.86 mg NO?-N/(L·h), and NO?-N concentration was below 0.16 mg/L. The formation of NH?-N was observed, but usually below 1.0 mg/L. Rapid biodegradation of starch on the surfaces of SPCL11 granules could cause an initial excess release of dissolved organic compound (DOC), and shortening HRT from 2h to 1h can result in sharp decrease of DOC.     

Using the combined bioelectrochemical and sulfur autotrophic denitrification system for groundwater denitrification

A combined bioelectrochemical and sulfur autotrophic denitrification system (CBSAD) was evaluated to treat a groundwater with nitrate contamination (20.9-22.0mgNO(3)(-)-N/L). The reactor was operated continuously for several months with groundwater to maximize treatment efficiency under different hydraulic retention times (HRT) and electric currents. The denitrification rate of sulfur autotrophic part followed a half-order kinetics model. Moreover, the removal efficiency of bioelectrochemical part depended on the electric current. The reactor could be operated efficiently at the HRT ranged from 4.2 to 2.1h (corresponding nitrogen volume-loading rates varied from 0.12 to 0.24 kg N/m(3)d; and optimum current ranged from 30 to 1000 mA), and the NO(3)(-)-N removal rate ranged from 95% to 100% without NO(3)(-)-N accumulation. The pH of effluent was satisfactorily adjusted by bioelectrochemical part, and the sulfate concentration of effluent was lower than 250 mg/L, meeting the drinking water standard of China EPA.     

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.     

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.     

固体发酵法固定工业废水处理优势菌的研究

为实现优势菌种的工程应用,由焦化废水处理站污泥筛选优势好氧菌A和兼性厌氧菌F,使用谷壳g、豆皮d为载体,采用固体发酵法进行固定化产品制备。初步研究表明固体发酵法固定菌种具有可行性,主要调控因素有温度、初始含水率、工业废水比例、pH、通风量和发酵时间。以pH8．0、温度好氧菌30℃（兼性厌氧菌35℃）、接种量1mL茴液儋田定化载体,初始含水量80％,固体发酵时间5d,低于60℃鼓风干燥,制备固定化产品。保存三个月,谷壳固定化产品好氧菌八的硝化能力和兼性厌氧菌R的反硝化能力不随保存时间的延长而改变;豆皮固定化产品氏、Fd降解能力随保存时问延长下降12％左右。以实验室岔／O工艺系统验证固定化产品处理焦化废水效果,缺氧池中无NO3-N积累,反硝化作用明显。氐和气对氰化物的去除率均达99％以上;对苯酚的去除效果气（98．84％）优于氏（79．6％）;但对NH4＋-N的去除率氏（75．46％）优于Ag（62．55％）。     

Ammonium oxidation via nitrite accumulation under limited oxygen concentration in sequencing batch reactors

In this study, the effects of sludge retention time (SRT) on NH(4)-N oxidation and NO(x)-N accumulation in the nitritation reactors were studied. The gradually decrease of SRT also caused long reaction time to achieve 99% NH(4)-N removal. Although the target NH(4)-N removal was achieved in a short reaction time at 40 days of SRT, decreasing of SRT from 40 to 30, 25, 20 days, increase the reaction time from 168 to 240 and 265 h, respectively. The inlet NH(4)-N was almost oxidized and the concentration of NO(2)-N accumulated to a high level of 177 mg/l, while NO(2)-N/(NO(3)-N+NO(2)-N) ratio was about 0.9 at SRT of 40 days. However, the concentration of NO(3)-N increased slightly and NO(2)-N/(NO(x)-N) ratio dropped to 0.8 when the SRT was lower than 40 days. During the operation in a cycle, free ammonia concentration in the SBR was decreased from 2.8 to 0.7 mg/l which is below the lowest concentration causing inhibition of nitrite oxidizing bacteria (NOB). It was assumed that combined dissolved oxygen limitation and NH(3)-N inhibition on NOB caused NO(2)-N accumulation under the experimental conditions.