吡啶缺氧生物降解特性及其降解产物

吡啶是焦化废水中较为典型的含氮杂环化合物,难以被生物降解。通过研究吡啶的缺氧生物降解特性,并对其降解产物进行鉴定,以期为实际生产提供理论依据和为今后进一步研究做出铺垫。结果表明,吡啶在本实验条件下的最佳降解浓度为80 mg·L~(-1),对于后期测定降解中间产物,该浓度和其降解周期均较为合适;戊二醛为吡啶在缺氧反硝化降解过程中的一个重要中间产物,其浓度在反应进行32 h时积累达到最大值。在上述实验基础上,在底物中加入40 mg·L~(-1)苯酚,其对吡啶的降解产生抑制作用,戊二醛浓度最大值出现在反应进行40 h处,由此推断苯酚对吡啶降解的抑制作用可能产生于吡啶开环脱氮阶段。     

同分异构体喹啉和异喹啉的缺氧降解性能比较

研究了同分异构体的含氮杂环化合物喹啉和异喹啉在缺氧条件下的降解情况,发现两者表现出不同的缺氧降解特性。喹啉可以在缺氧条件下得到有效降解,其缺氧降解的最佳碳氮比为8。在最佳碳氮比条件下,喹啉的缺氧降解过程符合一级动力学规律,在其降解过程中首先以硝酸盐为电子受体,当硝酸盐氮浓度为零时,亚硝酸盐氮浓度达到最高,此后喹啉的降解主要以亚硝酸盐为电子受体,并和亚硝酸盐氮同时达到最低浓度。异喹啉对硝酸盐的利用甚微,其降解主要表现为厌氧降解特征,降解过程符合零级动力学规律。     

水解酸化-缺氧法处理采油废水的污染物迁移降解试验研究

水解酸化-缺氧法对采油废水有较好的处理效果,采用GC/MS技术对水解酸化-缺氧法处理采油废水过程中污染物的迁移降解进行的研究表明:水解酸化段和缺氧段对采油废水中碳原子为C6～C9、分子量为100～140的有机物均有较好的降解能力.其中,在水解酸化段中酮类、芳烃得到较好的降解,缺氧段中酚类和醚类化合物降解明显.水解酸化-缺氧工艺对于采油废水中的甲苯和二甲苯具有较好的降解能力.     

水解酸化-缺氧法处理采油废水的污染物迁移降解试验研究

水解酸化．缺氧法对采油废水有较好的处理效果，采用GC／MS技术对水解酸化-缺氧法处理采油废水过程中污染物的迁移降解进行的研究表明：水解酸化段和缺氧段对采油废水中碳原子为C6-C9、分子量为100—140的有机物均有较好的降解能力。其中，在水解酸化段中酮类、芳烃得到较好的降解，缺氧段中酚类和醚类化合物降解明显。水解酸化-缺氧工艺对于采油废水中的甲苯和二甲苯具有较好的降解能力。     

微生物选育技术在废水生物处理中的应用进展

通过对微生物特别是细菌进行筛选和培育 ,可以得到降解能力强的高效菌株 ,将这些菌株应用于废水生物处理 ,能够增强废水处理工艺去除难降解有机污染物及削减其毒性的能力 ,本文对此进行了评述与展望。     

微生物选育技术在废水生物处理中的应用进展

通过对微生物特别是细菌进行筛选和培育,可以得到降解能力强的高效菌株,将这些菌株应用于废水生物处理,能够增强废水处理工艺去除难降解有机污染物及削减其毒性的能力,本文对此进行了评述的展望。     

对氯苯酚废水处理引起的活性污泥有机毒性

以处理难降解有机污染物对氯苯酚(4-CP)模拟废水的序批式好氧活性污泥系统为研究对象,探讨活性污泥在降解4-CP的过程中污泥有机毒性的形成与空间分布规律,以及污泥有机毒性随时间的变化趋势。处理组污泥用10 mg/L的4-CP模拟废水进行驯化。控制SBR系统的水力停留时间(HRT)和污泥停留时间(SRT)分别为12 h和20 d。结果表明,随着驯化时间的延长,处理组污泥毒性先升高后降低,最终达到稳定状态。在整个运行过程中,处理组污泥毒性始终高于对照组。4-CP的吸附与降解实验表明,污泥外层胞外聚集物(EPS)主要起吸附4-CP且向内层传递的作用,污泥有机毒性主要是由4-CP的降解过程引起,少部分由污染物吸附所致。     

新型活性炭固定化产品的制备及其处理焦化废水的特性

为解决优势菌种工程应用,研究不同固定化方法、载体和结构的固定化产品对焦化废水的降解特性。用活性炭粉末吸附菌种后,与聚乙烯醇和海藻酸钠混合制备了新型固定化球;用聚乙烯醇和海藻酸钠包埋吸附菌种的活性炭纤维毡,与立体弹性塑料填料连用,制备出3种不同形状的活性炭纤维膜片固定化产品复合填料。将游离菌和制备的4种活性炭固定化产品投入A/A/O工艺系统平行实验,考察处理焦化废水的效果。结果表明,活性炭纤维膜片固定化产品复合填料对焦化废水的降解能力优于其他固定化产品:缺氧池出水硝酸盐氮和亚硝酸盐氮浓度分别稳定在1.96 mg/L和0.49 mg/L,未产生氮的累积现象,COD去除率可达到60.92%。好氧池COD和氨氮降解效率分别为78.83%和85.52%,苯酚、氰化物降解效率均为97%以上。     

白腐菌在固体培养基下对吲哚和吡啶的降解

研究了稻草秆粉介质中白腐菌对吲哚和吡啶的降解.实验结果表明,质量浓度分别为200、80 mg/L左右的吲哚可被白腐菌去除99%以上,质量浓度为74 mg/L吡啶的去除率为61.5%;白腐菌在稻草秆粉培养体系中对吲哚和吡啶的降解,符合零级反应动力学,其中反应速率常数K(高浓度吲哚)＞K(低浓度吲哚)＞K(吡啶);高低浓度吲哚和吡啶3个降解体系的漆酶活力在第6天达到最大;漆酶在吲哚和吡啶降解过程中起着较重要的作用,但酶活的变化与吲哚和吡啶的相对去除率不呈线性相关,稻草秆粉培养基中的介质和培养环境在降解过程中可能也起着重要作用.     

固定化氧化还原介体加速亚硝酸盐生物反硝化作用

考察了利用循环伏安法所制备的固定化氧化还原介体(AQS/PPy/ACF)加速亚硝酸盐生物反硝化的特性,及其降解过程中pH和氧化还原电位(ORP)的变化特征。结果表明,AQS/PPy/ACF可显著地加速亚硝酸盐的生物降解;在不考虑各因子间交互作用的条件下,AQS/PPy/ACF加速亚硝酸盐降解的最佳条件为温度35℃,pH=8和碳氮比为6;AQS/PPy/ACF加速亚硝酸盐生物反硝化过程中pH的变化趋势与传统的亚硝酸盐生物反硝化过程中pH的变化趋势相似;AQS/PPy/ACF的加入可使亚硝酸盐生物反硝化过程中的ORP降低约45 mV;AQS/PPy/ACF具有较好的催化稳定性。本研究可为亚硝酸盐的生物降解提供新的技术途径,并为该技术的实际应用提供理论基础。     

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.     

利用亚硝酸盐为电子受体反硝化聚磷菌的筛选与富集

依据DPB原理,利用SBR动态反应器和静态释/聚磷装置.以A2/O工艺厌氧段污泥为种泥,研究以亚硝酸盐为电子受体反硝化聚磷菌的筛选与富集,同时对选择、富集污泥的反硝化聚磷性能进行了考察.结果表明:利用亚硝酸盐为电子受体的反硝化聚磷菌存在于A2/O厌氧段污泥中,通过厌氧/好氧和厌氧/缺氧方式运行后,聚磷菌总数由1400个/mL增加到32 000个/mL,其中反硝化聚磷菌占聚磷菌总数的比例也由14.5%提高到81%,磷酸盐和亚硝酸盐去除率分别由最初的8.65%和7.55%上升到91%和95.62%;筛选与富集利用亚硝酸盐为电子受体的反硝化聚磷菌时,缺氧段进水COD的浓度须控制在10 mg/L以下;当体系处于稳定状态,且亚硝酸盐氮浓度高达30 mg/L时,并未对反硝化聚磷菌的生存产生抑制和体系运行产生干扰,此时磷酸盐出水低至1.06 mg/L.     

好氧/缺氧消化降解污泥特征分析

为考察好氧/缺氧消化过程中污泥降解的特征,利用2个反应器进行对比试验,研究好氧/缺氧和好氧消化2个过程中VS的去除,pH和碱度变化,消化上清液中COD和氮元素变化等情况。试验结果表明:好氧/缺氧消化能够满足污泥稳定的要求,在常温条件下,消化16 d VS去除率即可达到38.2%,同时比好氧消化节约曝气能耗。好氧/缺氧消化对污泥中总氮的去除率高于传统的好氧消化,达到了36.4%,而且能够降低消化污泥上清液中的氨氮和硝态氮浓度。     

Treatability of nonylphenol ethoxylate surfactants in on-site wastewater disposal systems.

The fate of nine-mole nonylphenol ethoxylate (NPE9) discharged to an on-site wastewater disposal (septic) system was the focus of a 2-year investigation. Known amounts of NPE9-based detergent were metered daily into the plumbing at a single-family household. The ethoxylate-containing wastewater was discharged to the highly anoxic environment of a 4500-L septic tank before distribution to the oxic subsurface via 100 m of leach line. After 180 days of injecting detergent to the septic system, periodic soil pore water and/or groundwater samples were collected and analyzed for nonylphenol ethoxylates (NPEs), nonylphenol ether carboxylates, and nonylphenol. The NPE9 and degradation intermediates that were measured were reduced by 99.99% on a molar basis. An 18% reduction in molar concentration within the septic tank was observed. This was followed by a further 96.7% reduction of molar concentration within the leach lines. As the pore water migrated through the vadose zone, an additional 99.69% reduction in molar concentration was measured between the bottom of the leach lines (leach line effluent) and the lowest vadose zone monitoring location. The results obtained from these analyses indicate that degradation of the surfactant occurs within the anoxic portion of the disposal system with continued rapid biodegradation in the oxic unsaturated zone. Only trace amounts of degradation residuals were detected in soil pore water. The concentration and distribution of various degradation intermediates with respect to location, time, and ambient physical conditions were evaluated. Rapid and systematic degradation of NPE in on-site wastewater disposal systems was documented.     

Shewanellasp．XB缺氧反硝化降解苯酚

苯酚的生物降解一直受到关注。以苯酚为惟一电子供体,研究了Shewanellasp．XB对苯酚的缺氧降解特性。研究结果表明,在反硝化条件下,当C／N为13．3时,苯酚可以完全降解,NO2--N积累量很少。另外,当加入氧化还原介体,如核黄素3μmol／L、AQDS0．01mmol／L、AQS0．05mmol／L和LQ0．01mmol／L时,苯酚降解速率分别为不加介体时的1．45、1．77、1．67和1．63倍。当以氯化铵代替硝酸盐时,苯酚也能进行厌氧发酵降解。另外,菌株XB反硝化降解苯酚可能是厌氧和好氧降解的混合过程。     

Comparative abiotic or biotic degradation of carboxin by two Entisols with different surface properties or Pseudomonas aeruginosa strain: A toxicity study using the crustacean Thamnocephalus platyurus

The microcrustacean Thamnocephalus platyurus was used to detect the toxicity reduction of carboxin in abiotic degradation compared to biotic degradation. The abiotic degradation was obtained using two sterilized Entisols with different surface properties while the biotic degradation by Pseudomonas aeruginosa was obtained using the fungicide as the only C source. The results showed that the highest toxicity reduction rates for the abiotic degradation were achieved in 20 days with 49.2% for the coarser soil, 60.7% for the soil with a finer texture, whereas for the biotic degradation, 60.6%. Analysis (¹H NMR) showed that the soils transformed carboxin to produce sulfoxide and enol in different concentrations depending on the soil properties, while P. aeruginosa metabolized the fungicide to produce inorganic compounds such as ammonium and nitrite, minor degradation pathways were oxidized to sulfoxide and hydrolytic ring-opening to 2-[(2-hydroxyethyl)thio]acetoacetanilide enol. These results indicated that the degradation of carboxin occurred via abiotic catalytic processes as well as via biotic transformation leading to less toxic derivatives and such phenomena are caused by exchange/surface features of soils, rather than by the mere content of clay or organic matter fractions.     

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。     

Biodegradation of pentaerythritol tetranitrate (PETN) by anaerobic consortia from a contaminated site

This study examined the role of denitrifying and sulfate-reducing bacteria in biodegradation of pentaerythritol tetranitrate (PETN). Microbial inocula were obtained from a PETN-contaminated soil. PETN degradation was evaluated using nitrate and/or sulfate as electron acceptors and acetate as a carbon source. Results showed that under different electron acceptor conditions tested, PETN was sequentially reduced to pentaerythritol via the intermediary formation of tri-, di- and mononitrate pentaerythritol (PETriN, PEDN and PEMN). The addition of nitrate enhanced the degradation rate of PETN by stimulating greater microbial activity and growth of nitrite reducing bacteria that were responsible for degrading PETN. However, a high concentration of nitrite (350 mg L⁻¹) accumulated from nitrate reduction, consequently caused self-inhibition and temporarily delayed PETN biodegradation. In contrast, PETN degraded at very similar rates in the presence and absence of sulfate, while PETN inhibited sulfate reduction. It is apparent that denitrifying bacteria possessing nitrite reductase were capable of using PETN and its intermediates as terminal electron acceptors in a preferential utilization sequence of PETN, PETriN, PEDN and PEMN, while sulfate-reducing bacteria were not involved in PETN biodegradation. This study demonstrated that under anaerobic conditions and with sufficient carbon source, PETN can be effectively biotransformed by indigenous denitrifying bacteria, providing a viable means of treatment for PETN-containing wastewaters and PETN-contaminated soils.     

Nitrite reduction and formation of corrosion coatings in zerovalent iron systems

Batch tests were conducted to investigate nitrite reduction in a zerovalent iron (Fe0) system under various conditions. Nitrite at 1.4 mM initial concentration was slowly reduced to nitrogen gas in the first stage (days 1-6), which was mediated by an amorphous, Fe(II)-rich iron oxide coating. The second stage (days 7-14) featured a rapid reduction of nitrite to both ammonia and nitrogen gas and the formation of a more crystalline, magnetite form iron oxide coating. Water reduction by Fe0 occurred concurrently with nitrite reduction from the beginning and contributed significantly to the overall iron corrosion. Nitrite at 14 mM was found to passivate the surface of Fe0 grains with respect to nitrite reduction. Adding aqueous Fe2+ significantly accelerated reduction of nitrite by Fe0 to nitrogen gas with lepidocrocite as the main iron corrosion product. Substantially, though still substoichiometrically, 0.55 mol of Fe2+ were concomitantly consumed per 1.0 mol nitrite reduction, indicating that Fe0 was the main electron source. In the presence of Fe2+, nitrite reduction out-competed water reduction in terms of contributing to the overall iron corrosion. Results of this study help understand complicated interactions between water reduction and nitrite reduction, the roles of surface-bound Fe2+, and the evolution of the iron corrosion coating.