以吡啶、喹啉和吲哚为单一碳源时反硝化过程中亚硝酸盐积累及动力学研究

以吡啶、喹啉和吲哚为单一碳源,通过摇床实验进行反硝化过程动力学研究。实验结果表明,以吡啶和喹啉为单一碳源的反硝化过程中,NO-2-N的积累率分别达到了53.4%和16.4%;以吲哚为单一碳源的反硝化过程中,NO-2-N的积累现象不明显,最高不超过4%。以NO-3-N+0.6 NO-2-N作为反硝化电子受体,采用基于Monod方程的动态模型进行拟合,拟合曲线与实验测定值相关性良好。其次,采用基于Monod方程的微分方程组模型,也能够很好地拟合3种碳源条件下反硝化过程硝酸盐、亚硝酸盐质量浓度的变化,得到相应的动力学参数。     

硝酸盐对反硝化除磷过程的影响分析

在厌氧/缺氧间歇反应器内考察了硝酸盐进水浓度及进水方式对反硝化除磷过程的影响。结果表明：在缺氧阶段，反硝化除磷菌(DPBs)可将硝酸盐转化为亚硝酸盐，当硝酸盐浓度较低时，DPBs以亚硝酸盐为电子受体吸磷。进水COD浓度为220 mg/L，正磷浓度为6.8 mg/L，硝酸盐初始浓度为26 mg/L时，系统达到最佳脱氮除磷效果，期间亚硝酸盐浓度积累至10.71 mg/L。采用连续流投加硝酸盐的方式更利于氮磷的高效去除。     

共代谢基质对芽孢杆菌Y-4降解异喹啉的影响

以吡啶，葡萄糖和邻苯二甲酸作为共代谢基质，研究了它们对芽孢杆菌Y_4降解异喹啉的影响。实验结果表明各降解过程均遵循二级反应动力学方程：-dS／dt=K2S2＋K1S＋K0。吡啶的加入会抑制异喹啉的降解，并且吡啶的浓度越高，抑制作用越明显。反应体系中葡萄糖的浓度为100-800mg／L时，葡萄糖的加入会促进异喹啉的降解，且葡萄糖浓度越大，异喹啉降解速率P越大，当葡萄糖的浓度为800mg／L时，其降解率速率P可由未加葡萄糖的0．1924h。上升为0．2255h-1。适宜浓度的邻苯二甲酸会对异喹啉的降解产生促进作用，邻苯二甲酸的浓度为50mg／L时，异喹啉的降解速率可由原来的0．1924h-1增加到0．2145h-1，邻苯二甲酸浓度过高反而会抑制异喹啉的降解。     

低温喹啉降解菌的筛选及降解性能

从吉林石化污水处理厂的活性污泥中驯化、筛选获得一株降解效率高且生长速率快高效耐冷菌,命名为WS-5.该菌能以喹啉作为惟一的碳源、氮源及能源.结合菌体的形态观察、生理生化特性实验及16S rDNA序列同源性对比分析,鉴定菌株WS-5为恶臭假单胞菌(Pseudomonas putida).不同降解条件下的实验结果表明,菌株WS-5的最佳降解条件是投菌量为15％,pH值范围在8～10,摇床转速为100 r/min.最佳降解环境下对200 mg/L的喹啉在132 h降解率达到了85.3％.菌株WS-5对初始喹啉浓度为50、100、200和300 mg/L的初始喹啉浓度分别在36、72、192和262 h内完全降解.这将为今后在低温条件下处理含喹啉废水提供技术指导.     

氐温喹啉降解菌的筛选及降解性能

从吉林石化污水处理厂的活性污泥中驯化、筛选获得一株降解效率高且生长速率快高效耐冷菌，命名为WS-5。该菌能以喹啉作为惟一的碳源、氮源及能源。结合菌体的形态观察、生理生化特性实验及16SrDNA序列同源性对比分析，鉴定菌株WS-5为恶臭假单胞菌（Pseudomonasputida）。不同降解条件下的实验结果表明，菌株WS-5的最佳降解条件是投菌量为15％，pH值范围在8～10，摇床转速为100r／min。最佳降解环境下对200mg／L的喹啉在132h降解率达到了85．3％。菌株WS-5对初始喹啉浓度为50、100、200和300mg／L的初始喹啉浓度分别在36、72、192和262h内完全降解。这将为今后在低温条件下处理含喹啉废水提供技术指导。     

内循环管式光催化反应器降解水中喹啉的动力学研究

采用内循环管式光催化反应器,考察不同的温度、有机物底物浓度、光照强度、曝气强度等因素对水中喹啉的降解效果影响,在此基础上进行降解动力学研究。实验结果表明:温度、喹啉初始浓度、光照强度、曝气强度等因素与喹啉的催化降解呈现良好的相关关系,喹啉的表观吸附平衡常数为0.0244 L/mg,溶解氧表观吸附平衡常数为2.11,反应活化能为16.734 kJ/mol,光照强度修正指数为0.525。     

5种植物材料的水解释碳性能及反硝化效率

碳源在硝酸盐去除过程中起电子供体的作用,是生物反硝化反应的关键物质之一。为解决污水处理脱氮时碳源不足抑制反硝化反应造成脱氮效率低的问题,本研究选取风车草、甘蔗渣、芦竹、美人蕉和稻草秆5种植物材料作为反硝化碳源,探讨不同植物材料的水解释碳能力和释放规律;并进一步以其水解液作为外加碳源,探讨其对反硝化脱氮效率的影响。研究结果表明,植物材料水解释碳过程符合二级动力学反应规律,不同植物材料的释碳能力具有显著性差异,以甘蔗渣在固液比1∶80时COD释放当量最大,为45.45 mg/L;添加植物水解液可显著提高反硝化脱氮效率,以芦竹水解液脱氮效果最好,达到71.9%。此外,碳氮比是影响脱氮效率的重要因素之一,以碳氮比为9时反硝化脱氮效果最佳。     

八羟基喹啉改性膨润土预处理养殖废水

以八羟基喹啉为改性剂,天然膨润土为原料,制备一种新型吸附剂,并将其应用于养殖废水的预处理中。确定了改性膨润土的最佳制备条件:土液比为4 g/L,改性剂浓度为0.3 g/L,改性时间为50 min,改性温度为50℃。并以扫描电镜方法对改性膨润土行进表征:八羟基喹啉已经有效进入层间,改变了膨润土的性状,提高了吸附效果。优化了改性膨润土处理养殖废水的工艺条件:投土量为1 g/L,pH为4,搅拌时间为30 min,搅拌速度为350 r/min,沉淀时间为40 min。在此优化条件下,改性膨润土对养殖废水的COD去除率最高可达79.18%,且吸附动力学结果满足二级动力学模型。     

电子受体对深层土壤中石油烃缺氧降解的影响

微生物降解是处理土壤中石油烃(PHC)污染的有效技术,目前对PHC微生物降解的研究多集中在好氧条件下,对PHC缺氧微生物降解的研究较少,PHC缺氧降解规律尚不清楚。以PHC污染的深层土壤为对象,探究不同质量分数(500、1 500、5 000 mg·kg^-1)的硫酸盐、硝酸盐或混合电子受体对土壤中土著微生物丰度、群落结构以及PHC缺氧降解的影响规律。结果表明,150 d缺氧培养后,添加相同种类电子受体的土壤处理中细菌丰度、潜在PHC降解菌(变形菌门和厚壁菌门)丰度随电子受体的质量分数增加而增加;添加相同质量分数的不同种类电子受体土壤处理中细菌丰度、潜在PHC降解菌丰度从高到低分别为硝酸盐、混合电子受体、硫酸盐。添加相同种类电子受体的土壤处理中ΣPHC (C₁₀～C₃₀)和C1 (C₁₀～C₁₆)、C2 (C₁₇～C₂₃)、C3 (C₂₄～C₃₀)组分的降解率随着加入电子受体质量分数增加而增加...     

共基质对白腐菌降解喹啉的影响

选用吲哚、苯酚和氨氮作为喹啉降解的共基质.通过白腐菌BP对共基质的降解,研究了白腐菌BP对不同共基质降解体系中喹啉的降解过程及其反应动力学,同时研究了共基质物质对白腐菌BP漆酶活力、生物量增长速率和降解体系pH的影响.结果显示,白腐菌BP对不同共基质降解体系中的喹啉均具有较高的降解率,共基质物质苯酚、吲哚和氨氮对喹啉的降解有一定的抑制作用;共基质降解体系使白腐菌BP漆酶系统启动更加迅速,漆酶活力峰值提前出现;共基质降解体系能促进白腐菌BP的生长,缩短白腐菌BP的生长周期;秸秆滤出液培养基中,pH为6.00～8.00时,白腐菌BP对喹啉均具有较强的降解能力.     

A method for measuring the anoxic biodegradability under denitrifying conditions

A test for assessing the anoxic biodegradability of organic compounds under denitrifying conditions is proposed. The method is based on the recovery and quantification of the CO2 produced, which is evidence of complete biodegradation of the test compound (added as the sole carbon source). The tests were carried out in a mineral medium, with nitrate as electron acceptor. Whole lake sediments, sediment extracts and a commercial inoculum were assayed as a possible inoculum source by means of glucose biodegradability tests. It was found that the sediment extracts constitute a suitable and environmentally-relevant inoculum source, since they add non-significant amounts of carbon to the tests. Two xenobiotic compounds, namely, aniline and phenol, were tested in the aforementioned conditions as well as in a standard aerobic biodegradability test. Both aniline and phenol attained a biodegradation level higher than 60% in a short time period (<28 days) and thus can be considered as readily biodegradable in denitrifying environments. Nevertheless, the kinetics obtained in the anoxic test were slower than in aerobic conditions, and even suggested the accumulation of intermediate metabolites in the case of phenol. The results of this study indicate that the fate of xenobiotic compounds under anoxic conditions differs from that observed in an oxic environment, and therefore it should be considered by standard biodegradability testing procedures.     

Anaerobic nonylphenol ethoxylate degradation coupled to nitrate reduction in a modified biodegradability batch test

The aim of this work was to elucidate the role of nitrate as a terminal electron acceptor on the biodegradation of NPEO. We have characterized the products of NPEO degradation by mixed microbial communities in anaerobic batch tests by means of HPLC, ¹H NMR and GC–MS. Anaerobic degradation of NPEO was strictly dependent on the presence of nitrate. Within seven days of anoxic incubation, NP2EO appeared as the major degradation product. After 21 days, NP was the main species detected, and was not degraded further even after 35 days. Nitrate concentration decreased in parallel with NPEO de-ethoxylation. A transient accumulation of nitrite was observed within the time period in which NP formation reached its maximum production. The observed generation of nonylphenol coupled to nitrate reduction suggests that the microbial consortium possessed an alternate pathway for the degradation of NPEO, which was not accessible under aerobic conditions.     

Anaerobic decomposition of halogenated aromatic compounds

Halogenated compounds constitute one of the largest groups of environmental pollutants, partly as a result of their widespread use as biocides, solvents and other industrial chemicals. A critical step in degradation of organohalides is the cleavage of the carbon?halogen bond. Reductive dehalogenation is generally the initial step in metabolism under methanogenic conditions, which requires a source of reducing equivalents, with the halogenated compound serving as an electron acceptor. Dehalogenation is greatly influenced by alternate electron acceptors; e.g. sulfate frequently inhibits reductive dehalogenation. On the other hand, a number of halogenated aromatic compounds can be degraded under different electron-accepting conditions and their complete oxidation to CO(2) can be coupled to processes such as denitrification, iron(III)-reduction, sulfate reduction and methanogenesis. Reductive dehalogenation was the initial step in degradation not only under methanogenic, but also under sulfate- and iron(III)-reducing conditions. Dehalogenation rates were in general slower under sulfidogenic and iron-reducing conditions, suggesting that dehalogenation was affected by the electron acceptor. The capacity for dehalogenation appears to be widely distributed in anoxic environments; however, the different substrate specificities and activities observed for the halogenated aromatic compounds suggest that distinct dehalogenating microbial populations are enriched under the different reducing conditions. Characterization of the microbial community structure using a combination of biomolecular techniques, such as cellular fatty acid profiling, and 16 S rRNA fingerprinting/sequence analysis, was used to discern the distinct populations enriched with each substrate and under each electron-accepting condition. These combined techniques will aid in identifying the organisms responsible for dehalogenation and degradation of halogenated aromatic compounds.     

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.     

Concurrent nitrate and Fe(III) reduction during anaerobic biodegradation of phenols in a sandstone aquifer

The biodegradation of phenols (5, 60, 600 mg l⁻¹) under anaerobic conditions (nitrate enriched and unamended) was studied in laboratory microcosms with sandstone material and groundwater from within an anaerobic ammonium plume in an aquifer. The aqueous phase was sampled and analyzed for phenols and selected redox sensitive parameters on a regular basis. An experiment with sandstone material from specific depth intervals from a vertical profile across the ammonium plume was also conducted. The miniature microcosms used in this experiment were sacrificed for sampling for phenols and selected redox sensitive parameters at the end of the experiment. The sandstone material was characterized with respect to oxidation and reduction potential and Fe(II) and Fe(III) speciation prior to use for all microcosms and at the end of the experiments for selected microcosms.The redox conditions in the anaerobic microcosms were mixed nitrate and Fe(III) reducing. Nitrate and Fe(III) were apparently the dominant electron acceptors at high and low nitrate concentrations, respectively. When biomass growth is taken into account, nitrate and Fe(III) reduction constituted sufficient electron acceptor capacity for the mineralization of the phenols observed to be degraded even at an initial phenols concentration of 60 mg l⁻¹ (high) in an unamended microcosm, whereas nitrate reduction alone is unlikely to have provided sufficient electron acceptor capacity for the observed degradation of the phenols in the unamended microcosm.For microcosm systems, with solid aquifer materials, dissolution of organic substances from the solid material may occur. A quantitative determination of the speciation (mineral types and quantity) of electron acceptors associated with the solids, at levels relevant for degradation of specific organic compounds in aquifers, cannot always be obtained. Hence, complete mass balances of electron acceptor consumption for specific organic compounds degradation are difficult to confine. For aquifer materials with low initial Fe(II) content, Fe(II) determinations on solids and in aqueous phase samples may provide valuable information on Fe(III) reduction. However, in microcosms with natural sediments and where electron acceptors are associated with the sediments, complete mass-balances for substrates and electron acceptors are not likely to be obtained.     

Microbial degradation of methyl tert-butyl ether and tert-butyl alcohol in the subsurface

The fate of fuel oxygenates such as methyl tert-butyl ether (MTBE) in the subsurface is governed by their degradability under various redox conditions. The key intermediate in degradation of MTBE and ethyl tert-butyl ether (ETBE) is tert-butyl alcohol (TBA) which was often found as accumulating intermediate or dead-end product in lab studies using microcosms or isolated cell suspensions. This review discusses in detail the thermodynamics of the degradation processes utilizing various terminal electron acceptors, and the aerobic degradation pathways of MTBE and TBA. It summarizes the present knowledge on MTBE and TBA degradation gained from either microcosm or pure culture studies and emphasizes the potential of compound-specific isotope analysis (CSIA) for identification and quantification of degradation processes of slowly biodegradable pollutants such as MTBE and TBA. Microcosm studies demonstrated that MTBE and TBA may be biodegradable under oxic and nearly all anoxic conditions, although results of various studies are often contradictory, which suggests that site-specific conditions are important parameters. So far, TBA degradation has not been shown under methanogenic conditions and it is currently widely accepted that TBA is a recalcitrant dead-end product of MTBE under these conditions. Reliable in situ degradation rates for MTBE and TBA under various geochemical conditions are not yet available. Furthermore, degradation pathways under anoxic conditions have not yet been elucidated. All pure cultures capable of MTBE or TBA degradation isolated so far use oxygen as terminal electron acceptor. In general, compared with hydrocarbons present in gasoline, fuel oxygenates biodegrade much slower, if at all. The presence of MTBE and related compounds in groundwater therefore frequently limits the use of in situ biodegradation as remediation option at gasoline-contaminated sites. Though degradation of MTBE and TBA in field studies has been reported under oxic conditions, there is hardly any evidence of substantial degradation in the absence of oxygen. The increasing availability of field data from CSIA will foster our understanding and may even allow the quantification of degradation of these recalcitrant compounds. Such information will help to elucidate the crucial factors of site-specific biogeochemical conditions that govern the capability of intrinsic oxygenate degradation.     

Bioremediation of chlorobenzene-contaminated ground water in an in situ reactor mediated by hydrogen peroxide

New in situ reactive barrier technologies were tested nearby a local aquifer in Bitterfeld, Saxonia-Anhalt, Germany, which is polluted mainly by chlorobenzene (CB), in concentrations up to 450 microM. A reactor filled with original aquifer sediment was designed for the microbiological remediation of the ground water by indigenous bacterial communities. Two remediation variants were examined: (a) the degradation of CB under anoxic conditions in the presence of nitrate; (b) the degradation of CB under mixed electron acceptor conditions (oxygen+nitrate) using hydrogen peroxide as the oxygen-releasing compound. Under anoxic conditions, no definite degradation of CB was observed. Adding hydrogen peroxide (2.94 mM) and nitrate (2 mM) led to the disappearance of CB (ca. 150 microM) in the lower part of the reactor, accompanied by a strong increase of the number of cultivable aerobic CB degrading bacteria in reactor water and sediment samples, indicating that CB was degraded mainly by productive bacterial metabolism. Several aerobic CB degrading bacteria, mostly belonging to the genera Pseudomonas and Rhodococcus, were isolated from reactor water and sediments. In laboratory experiments with reactor water, oxygen was rapidly released by hydrogen peroxide, whereas biotic-induced decomposition reactions of hydrogen peroxide were almost four times faster than abiotic-induced decomposition reactions. A clear chemical degradation of CB mediated by hydrogen peroxide was not observed. CB was also completely degraded in the reactor after reducing the hydrogen peroxide concentration to 880 microM. The CB degradation completely collapsed after reducing the hydrogen peroxide concentration to 440 microM. In the following, the hydrogen peroxide concentrations were increased again (to 880 microM, 2.94 mM, and 880 microM, respectively), but the oxygen demand for CB degradation was higher than observed before, indicating a shift in the bacterial population. During the whole experiment, nitrate was uniformly reduced during the flow path in the reactor.     

反硝化聚磷机理试验

通过实验研究缺氧反硝化聚磷 ,揭示DPB细菌在厌氧和缺氧交替环境下的厌氧释磷、缺氧反硝化吸磷及CODCr变化规律。结果表明 ,DPB细菌在缺氧条件下可利用NO-3 作最终电子受体进行吸磷 ,其吸磷效果及反硝化速率高于常规脱氮除磷工艺。     

The effect of residual chemical oxygen demand on anoxic and aerobic phosphate uptake and release with various intracellular polymer levels.

This study investigated the anoxic and aerobic phosphate uptake and release reactions and the fraction of denitrifying phosphate-accumulating organisms (DPAOs) under various initial chemical oxygen demand (COD) and residual COD conditions. The results showed that DPAOs and non-DPAOs could release phosphate when high soluble COD was present. Consequently, the phosphate-uptake potential was dynamic and increased when the initial COD increased, the initial polyhydroxyalkanoates (PHA) increased, and the residual COD decreased. Furthermore, the electron acceptor (oxygen of nitrate) has more significant influence on the phosphate uptake/release characteristics, while the residual COD concentrations have little influence on that. The fraction of DPAOs to phosphate-accumulating organisms was 42% when the initial PHA storage was enough by both DPAOs and non-DPAOs. This was closely related to the relative phosphate uptake (47%) in the anoxic zone of the process.     

Toxicity change patterns and its mechanism during the degradation of nitrogen-heterocyclic compounds by O(3)/UV

Many nitrogen-heterocyclic compounds (NHCs) are toxic and recalcitrant contaminants that need to be degraded by advanced oxidation processes. In this study, quinoline, isoquinoline and indole were selected to investigate their toxicity patterns during the degradation by O(3)/UV. It was found that for all the three NHCs there was some H(2)O(2) formed in the degradation process, which caused the sharp increase of toxicity to Photobacterium phosphoreum. The toxicity decreasing patterns after H(2)O(2) elimination were different for quinoline (or isoquinoline) and indole. After H(2)O(2) elimination, for quinoline or isoquinoline the toxicity decreased concurrently with the decrease of its concentration, while for indole the toxicity lagged behind its removal rate. The rate constant of the NHC with O(3) (k(D)) was the decisive parameter of its toxicity pattern because of its critical role in determining the degradation rate of the NHC. Two quantitative structure-activity relationship equations for the k(D) values of simple NHCs and homocyclic aromatics were successfully established, which would be useful to predict their toxicity patterns.