Cr（Ⅵ）对活性污泥系统反硝化过程的影响

采用反硝化反应器,研究了Cr（Ⅵ）对活性污泥系统反硝化过程的影响。在进水Cr（Ⅵ）投加量2.5 mg/L条件下,活性污泥反硝化过程中COD和硝酸盐氮的去除率受到的影响较小,而在10.0 mg/L条件下受到的影响较大,COD和硝酸盐氮的去除率分别从最初的97.1%和99.0%降至70.6%和24.7%。在停止投加Cr（Ⅵ）后的恢复期内,反硝化系统可以逐渐恢复对COD和硝酸盐氮的去除,亚硝酸盐氮仍会有积累,但随着时间的延长可恢复至初始状态。硝酸盐氮还原为亚硝酸盐氮的过程比亚硝酸盐氮的还原过程更易受到Cr（Ⅵ）的影响。     

基于固态碳源的自养-异养耦合生物脱氮工艺研究

采用基于固态碳源的厌氧氨氧化与反硝化耦合脱氮工艺处理高氮低碳的金属热处理废水。通过接种城市生活污水处理厂剩余污泥和厌氧氨氧化絮状污泥,研究了以固态碳源（3-羟基丁酸脂和3-羟基戊酸脂共聚物,PHBV）和沸石为组合填料的分区式耦合反应器的启动和运行特性。经过76 d的运行,耦合反应器的总氮去除速率达1.05 kg/（m³·d）,且具有良好的出水COD稳定性。废水经过反应器沸石区后,氨氮去除率达97%,亚硝态氮去除率达81%,而硝态氮去除率几乎为零;经过PHBV区后,硝态氮去除率达76%,亚硝态氮去除率达99%,氨氮去除率达97%。沸石区主要进行厌氧氨氧化反应,PHBV区主要进行反硝化反应,功能分区明确,耦合效果较好。     

Nitrate enhancement of in-situ bioremediation of monoaromatic compounds in groundwater

Removal of benzene, toluene, and the isomers of xylene (BTX) from gasoline-contaminated groundwater under denitrifying conditions was investigated. In laboratory microcosms, benzene removal was found to be significantly stimulated by phosphorus addition. For total xylenes, removal followed a similar response, but toluene disappearance was unaffected by phosphorus enrichment. An in-situ bioremediation project was conducted to extend this laboratory work to an actual field-scale cleanup of gasoline-contaminated groundwater. The flow of groundwater from two extraction wells to an infiltration gallery created a mostly closed loop to recycle the groundwater enriched with added nutrients and the electron acceptor (nitrate). The coincident occurrence of BTX loss (greater than 90 percent) in situ, nitrate (as well as phosphorus and ammonia) appearance, and increased levels of denitrifying bacteria at a downgradient well all suggested that denitrification may play a significant role in BTX remediation at this site.     

Anaerobic microbial degradation of poly (3-hydroxyalkanoates) with various terminal electron acceptors

The microbial degradation of poly (3-hydroxyalkanoates) (PHAs) under anaerobic conditions with various terminal electron acceptors was examined. Nitrate-reducing consortia were established using activated sludge, and PHAs were shown to be biodegradable under these conditions. A positive correlation between carbon dioxide production and nitrate reduction was demonstrated. Nitrous oxide accumulated as the main N-containing product of nitrate reduction. The amount of PHAs in activated sludge cultures decreased approximately 20% within 40 days of incubation. Attempts were made to establish iron- and sulfate-reducing consortia from spring water, yet it could not be demonstrated that the mixed cultures were capable of degrading PHAs. Pure cultures of iron- and sulfate-reducing bacteria could not utilize PHAs as sole carbon sources. Methanogenic environments sampled included pond sediment and rumen fluid. PHAs were fermented to methane and carbon dioxide after 10 weeks by a sediment consortium, with 43 to 57% of the substrate carbon transformed to methane. Although it could not be demonstrated that PHAs were biodegraded by a rumen fluid consortium, a facultative anaerobic bacterium, identified as aStaphylococcus sp., that could grow on PHAs was isolated from rumen fluid.     

Organic and nitrogen removal from landfill leachate in aerobic granular sludge sequencing batch reactors

Granule sequencing batch reactors (GSBR) were established for landfill leachate treatment, and the COD removal was analyzed kinetically using a modified model. Results showed that COD removal rate decreased as influent ammonium concentration increasing. Characteristics of nitrogen removal at different influent ammonium levels were also studied. When the ammonium concentration in the landfill leachate was 366 mg L⁻¹, the dominant nitrogen removal process in the GSBR was simultaneous nitrification and denitrification (SND). Under the ammonium concentration of 788 mg L⁻¹, nitrite accumulation occurred and the accumulated nitrite was reduced to nitrogen gas by the shortcut denitrification process. When the influent ammonium increased to a higher level of 1105 mg L⁻¹, accumulation of nitrite and nitrate lasted in the whole cycle, and the removal efficiencies of total nitrogen and ammonium decreased to only 35.0% and 39.3%, respectively. Results also showed that DO was a useful process controlling parameter for the organics and nitrogen removal at low ammonium input.     

Nitrogen management in bioreactor landfills

One scenario for long-term nitrogen management in landfills is ex situ nitrification followed by denitrification in the landfill. The objective of this research was to measure the denitrification potential of actively decomposing and well decomposed refuse. A series of 10-l reactors that were actively producing methane were fed 400 mg NO3-N /l every 48 h for periods of 19-59 days. Up to 29 nitrate additions were either completely or largely depleted within 48 h of addition and the denitrification reactions did not adversely affect the leachate pH. Nitrate did inhibit methane production, but the reactors recovered their methane-producing activity with the termination of nitrate addition. In well decomposed refuse, the nitrate consumption rate was reduced but was easily stimulated by the addition of either acetate or an overlayer of fresh refuse. Addition of acetate at five times the amount required to reduce nitrate did not lead to the production of NH4+ by dissimilatory nitrate reduction. The most probable number of denitrifying bacteria decreased by about five orders of magnitude during refuse decomposition in a reactor that did not receive nitrate. However, rapid denitrification commenced immediately with nitrate addition. This study shows that the use of a landfill as a bioreactor for the conversion of nitrate to a harmless byproduct, nitrogen gas, is technically viable.     

Atmospheric Deposition of Reactive Nitrogen on Turf Grassland in Central Japan: Comparison of the Contribution of Wet and Dry Deposition

The atmospheric deposition of reactive nitrogen on turf grassland in Tsukuba, central Japan, was investigated from July 2003 to December 2004. The target components were ammonium, nitrate, and nitrite ions for wet deposition and gaseous ammonia, nitric and nitrous acids, and particulate ammonium, nitrate, and nitrite for dry deposition. Organic nitrogen was also evaluated by subtracting the amount of inorganic nitrogen from total nitrogen. A wet-only sampler and filter holders were used to collect precipitation and the atmospheric components, respectively. An inferential method was applied to calculate the dry deposition velocity of gases and particles, which involved the effects of surface wetness and ammonia volatilization through stomata on the dry deposition velocity. The mean fraction of the monthly wet to total deposition was different among chemical species; 37, 77, and 1% for ammoniacal, nitrate-, and nitrite-nitrogen, respectively. The annual deposition of inorganic nitrogen in 2004 was 47 and 48 mmol m⁻² yr⁻¹ for wet and dry deposition, respectively; 51% of atmospheric deposition was contributed by dry deposition. The annual wet deposition in 2004 was 20, 27, and 0.07 mmol m⁻² yr⁻¹, and the annual dry deposition in 2004 was 35, 7.4, and 5.4 mmol m⁻² yr⁻¹ for ammoniacal, nitrate-, and nitrite-nitrogen, respectively. Ammoniacal nitrogen was the most important reactive nitrogen because of its remarkable contribution to both wet and dry deposition. The median ratio of the organic nitrogen concentration to total nitrogen was 9.8, 17, and 15% for precipitation, gases, and particles, respectively.     

制药废水硝化-反硝化除氮研究

含高浓度氮的制药废水经好氧生化处理后,虽然出水的ＣＯＤ,ＢＯＤ５均可达到行业排放标准,但ＴＮ仍高达约１７０ｍｇ／Ｌ。本研究在曝气池中设置填料,利用生物膜外层好氧,内层缺氧厌氧的条件,使硝化－反硝化脱氮在同一构筑物内进行,ＮＨ３－Ｎ和ＴＮ去除率分别可达约９０％和７０％。在本试验条件范围内,温度越高,负荷越低,硝化和反硝化作用越完全,ＮＨ３－Ｎ和ＴＮ去除率越高。     

Combinations of Horizontal and Vertical Flow Constructed Wetlands to Improve Nitrogen Removal

Nitrogen removal in wetlands is achieved through two pathways: (a) N cycling and (b) storage. N cycling is a permanent removal pathway. There has been an increasing interest in the development of technologies to alleviate permanent nitrogen removal limitation in constructed wetlands by ensuring prevalence of conditions enhancing N cycling. The purpose of this study is to review an emerging technology of vegetated submerged bed constructed wetland system aimed at improving nitrogen removal in wetlands through rational system design. The design and performance of this system type is evaluated. The oxygen transfer capacity and nitrogen removal mechanisms on system performance are evaluated. Constructed wetland combinations most commonly consist of vertical flow (VF) and horizontal flow (HF) beds where VF and HF are aimed at nitrification and denitrification, respectively. Nitrate nitrogen accumulation is the most limiting factor in typical VF based systems.     

Heterotrophic Biological Denitrification Using Microbial Cellulose as Carbon Source

The objective of this study was to investigate the feasibility of using a microbial biopolymer produced by Acetobacter xylinum as a carbon source for heterotrophic biological denitrification. The denitrification rate, COD availability and nitrite concentration were response parameters. Under the experimental conditions, a denitrification rate of about 0.74 kg NO₃ ⁻N/m³d at 6 h retention time was achieved with microbial cellulose (MC). The reactor effluent contained significantly COD concentrations (20–86 mg/L) so it was not carbon limited, and was receiving enough carbon to facilitate the denitrification process. The maximum nitrite concentration in the effluent was found to be 0.4 mg/L. However, decreasing the retention time to 3 h significantly reduced the efficiency. It can be concluded that the MC is a suitable carbon source for nitrate removal in a heterotrophic biological denitrification process.     

Treatment of acid lignite mine flooding water by means of microbial sulfate reduction

During and after mining activities acidic waters containing high amounts of heavy metals and sulfate often occur. In addition to precipitation processes, water purification is also possible with the help of sulfate-reducing bacteria (SRB). A mixed culture of SRB was adapted to methanol as a cheap carbon source. In order to receive high sulfate-reduction rates immobilization on porous materials proved to be advantageous. Continuous laboratory experiments based on immobilized SRB were carried out with original water from a lignite mining site reaching sulfate-reducing rates up to 132 mg SO4(2-)/(1 h). Based on these results a process for the treatment of such waters was designed. Heavy metals are removed by recycling sulfide containing effluent, excess sulfide can be oxidized to elemental sulfur by addition of hydrogen peroxide. The plant with a 3.9 m3 bioreactor with immobilized SRB was constructed at the mine site. This pilot plant was operated successfully for some months. The removal of heavy metals was close to 100%, the pH of the acidic water increased from 3.0 to 6.9. The sulfate-reducing rate again reached 134 mg SO4(2-)/(1 h). The production of sulfur from the excess sulfide is possible.     

烟气中NOx脱除技术的研究进展

综述了干法脱硝、湿法脱硝、微生物法和化学吸收-生物还原法脱除烟气中氮氧化物的原理、技术特点和存在的问题。指出：化学吸收-生物还原法是未来脱除烟气中氮氧化物的主要研究方向之一,可通过提高NO在水中的溶解性,利用微生物去除氮氧化物,力争将其从实验室研究推广至工业应用。     

硫酸盐对微生物燃料电池脱氮的影响

构建了双室型微生物燃料电池(MFC),探讨了硫酸盐对MFC阴极脱氮效果和产电性能的影响。实验结果表明:缺氧阴极室中,硝酸盐氮、硫酸盐的还原存在一定的竞争关系,且硫酸盐对电子的竞争能力比硝酸盐氮强;当S与N的质量比(记为S/N)为2∶1时,72 h后的硫酸根去除率达96.41%,而硝酸盐氮去除率仅为36.86%;在S/N为2∶1的条件下,当电压达307.6 m V时,功率密度达最大值15.77 W/m2,电池内阻为100Ω,与未加入硫酸盐时相比产电性能明显提高。     

分子筛催化剂生产废水的生物处理

采用氨化—硝化—反硝化三段联合生物工艺处理分子筛催化剂生产过程中产生的含有机胺废水。实验结果表明：在氨化过程中,当进水COD稳定为1 200~1 600 mg/L时,出水COD低于300 mg/L,COD去除率稳定在80%左右,当进水ρ（有机氮）为100~160 mg/L时,出水ρ（有机氮）均低于30 mg/L,有机氮去除率大于80%,在整个氨化过程中,出水ρ（氨氮）较进水ρ（氨氮）提高了35~200 mg/L;硝化过程中,当进水ρ（氨氮）小于等于300 mg/L时,出水ρ（氨氮）最终稳定在15 mg/L以内,氨氮去除率大于90%;在反硝化过程中,亚硝酸盐氮去除率基本稳定在98%以上,最终出水COD低于80 mg/L,出水ρ（总氮）低于25 mg/L。     

ClO_2溶液去除烟气中NO的效果及工程应用

采用实验室规模喷淋脱硝装置对ClO_2溶液去除NO的效果及影响因素进行探讨,通过脱硝产物的测定对ClO_2溶液去除NO的能力及机理进行分析;在此基础上考察ClO_2溶液对供热厂燃煤锅炉烟气的实际脱硝效果。实验结果表明:在液气比为20L/m~3、反应温度为20℃,反应pH为4.0、进气NO质量浓度为250 mg/m~3,ClO_2质量浓度为200 mg/L的条件下,NO去除率达97%以上;ClO_2溶液可将NO氧化吸收为NO_3~-,氧化后产生的NO_x也可被NaOH溶液吸收转化为NO_2~-和NO_3~-;在ClO_2质量浓度为200~500 mg/L,反应pH为5.5~7.0的条件下处理初始NO质量浓度为212~230 mg/m~3的燃煤锅炉烟气,NO去除率为85.7%~94.6%,NO_x去除率为80.4%~88.8%,出口NO_x质量浓度低于46 mg/m~3,远低于GB 13271—2014规定的排放限值。     

改性沸石复合材料的制备及对废水同步脱氮除磷

采用十六烷基三甲基溴化铵(HDTMA)溶液和LaCl3溶液对人造沸石进行改性,以实现其对废水的同步脱氮除磷。通过正交试验确定了改性沸石制备的最佳条件,并运用SEM、BET、EDS、FTIR、XRD和TG技术对改性沸石进行了表征。实验结果表明:改性可提高人造沸石对废水中氨氮(NH4+-N)和总磷(TP)的去除率;改性沸石制备的最佳条件为HDTMA质量浓度12 g/L、LaCl3质量浓度9 g/L、HDTMA溶液和LaCl3溶液的体积比1∶5,固液比1∶90;采用该条件下制备的改性沸石吸附处理NH4+-N和TP的质量浓度分别为23.78 mg/L和11.78 mg/L的废水,NH4+-N和TP的去除率分别达96.88%和95.12%。表征结果显示,改性后,HDTMA和LaCl3有效负载于人造沸石表面,且未改变人造沸石的基本骨架。     

厌氧氨氧化技术在废水脱氮领域的应用进展

厌氧氨氧化技术是一种以厌氧氨氧化自养菌脱氮为核心的新型生物脱氮技术,具有良好的应用前景。本文对厌氧氨氧化过程的反应机理、菌种的生长特性及种类分布进行了详细介绍,总结了厌氧氨氧化技术在不同废水脱氮领域的研究及应用情况。指出,种泥缺乏是当前限制厌氧氨氧化技术大规模工业推广的瓶颈,并就厌氧氨氧化技术在应用过程中遇到的问题给出了相应建议。     

Biodegradation of Slow-Release Fertilizers (Methyleneureas) in Soil

The biodegradation of urea and condensation products thereof (ureaforms or methyleneureas), their nitrification, and their influence on the respiratory rate of soil was studied over periods of up to 100 days. The total methyleneurea content of the soil was determined after its acidic extraction, using a convenient colorimetric assay, and an HPLC protocol was established to analyze for specific components of methyleneureas. Urea, unfractionated methyleneureas, and hot-water soluble methyleneureas were rapidly metabolized to ammonium, which accumulated to high concentrations and was consequently oxidized to nitrate; an accumulation of nitrite was observed during urea but not during methyleneurea degradation. Hot water-insoluble methyleneureas were degraded much more slowly, and ammonium formed from these compounds was oxidized to nitrate without being released in significant amounts. These results suggest that the use of methyleneureas of optimized composition with regard to their water solubility may help to resolve problems such as the toxicity of ammonia to plant growth as well as nitrogen loss by leaching of nitrate, denitrification and volatilization.     

pH对厌氧氨氧化反应脱氮效能的影响

采用具有恒定pH功能的SBR接种厌氧氨氧化颗粒污泥,研究了pH对厌氧氨氧化菌脱氮效能的影响。实验结果表明:在进水ρ(氨氮)和ρ(亚硝酸盐氮)分别为58.00 mg/L和79.28 mg/L、TN容积负荷为0.82 kg/(m3·d)、不控制反应pH的条件下,随着反应的进行,pH不断升高,当pH=8.02时,菌种的去除效能最高;在进水ρ(氨氮)和ρ(亚硝酸盐氮)分别为120.00 mg/L和159.33 mg/L、TN容积负荷为1.62 kg/(m3·d)、恒定反应pH为8.00的条件下,反应4.0 h时的容积基质氮去除速率(NRR)达到1.42 kg/(m3·d),氨氮去除率达98.39%,亚硝酸盐氮去除率达99.48%;拟合曲线推导的最适pH的理论值为7.85,反应4.0 h时的NRR理论最大值达1.52 kg/(m3·d)。     

厌氧／好氧生物脱氮－絮凝法处理焦化废水

采用厌氧／好氧生物脱氨－絮凝法处理焦化废水，出水中ＮＨ＿３－Ｎ＜１５ｍｇ／Ｌ，ＣＯＤ为９６－１５８ｍｇ／Ｌ。利用甲醇残液及其他有机废水作为外加碳源，可以达到以废治废的目的。