钟落潭种猪场污水的活性污泥法处理

钟落潭种猪场日排放COD值为15000mg·L^-1以上的有机污水约150m³·d^-1,污水处理设计采用水解酸化-传统活性污泥-兼性塘组合方法,原污水经过粗格网筛、调解池、细格阿筛、水解酸化池、一级沉淀池、二级沉淀池、集水池、曝气池、二沉池和缓冲池,最后流入兼性塘,活性污泥通过污泥于化场得到干化.整个污水处理部分占地约150m×50m,兼性塘占地约6000m²,系统正常运行后处理水可以达到“污水综合排放标准(GB8978-1996)”中规定的二级标准.     

PCR-DGGE技术分析染整废水微生物群落多样性

旨在揭示水解酸化-生物接触氧化工艺处理染整废水过程中的微生物多样性.取初级沉淀池,水解酸化池,生物接触氧化池和二沉池的活性污泥,通过细胞裂解直接提取基因组DNA,以细菌通用引物进行16S rRNA基因V3区域PCR扩增,将PCR产物进行变性梯度凝胶电泳,获得微生物群落的DNA特征指纹图谱,并对条带进行统计分析和切胶测序,进行了同源性分析并建立了系统发育树.研究表明,整个水处理过程中含有丰富的微生物群落,其中初级沉淀池、水解酸化池、二沉池和生物接触氧化池的污泥样品分别测出36条带、42条带、30条带和29条带.不同区段微生物群落间相似度最高达68％,最低达42.4％,说明群落间演替明显,不同工艺区段既存在共同的微生物种属也存在特异微生物种属.     

两个污水处理系统的能值与经济综合分析

运用改进的能值评价指标和经济指标对构建的两个污水处理综合系统("污水处理厂处理+脱水污泥填埋"及"污水处理厂处理+脱水污泥填埋+中水回用")进行了环境可持续性和经济竞争力的综合分析。改进的能值指标(能值产出率SEYR、环境负载率SELR、环境可持续发展指数SESI和能值受益率SEBR)是在考虑研究对象废物及产物能值对环境影响的基础上提出的,更好地反映了系统的特征。结果表明,中水回用系统的增加有利于提升系统的环境可持续发展能力;"污水处理厂处理+脱水污泥填埋+中水回用"系统较"污水厂处理+脱水污泥填埋"系统的经济竞争力差,但却拥有更强的可持续发展能力,有利的经济政策能够刺激其更好的推广运用。     

大庆石化用生物技术除臭

大庆石化水气厂采用生物式空气净化工艺,治理污水毒气取得突破性进展。总投资500多万元的化工、腈纶毒气治理装置处理量为2 000 m3/h的装置,主要处理化工原水池、污泥浓缩池、腈纶缺氧池、曝气池混合室等7处污水池产生的恶臭气体。该系统利用微生物降解恶臭物质,使之成为氧化产物。被降解的含硫化氢的臭气首先溶解于喷淋池中,再通过固定化生物滤料的氧化,将臭气中的H2S氧化为硫酸盐,有机臭气氧化为CO2和水,在该厂污水车间投用后,H2S、氰化氢、苯三大污染物出口合格率实现100%。环保监测站采样分析表明,该装置投用后,每年可减排H2S 168 kg、氰化氢14 kg、苯65 kg。大庆石化用生物技术除臭     

厌氧氨氧化颗粒污泥聚集机制研究进展

厌氧氨氧化(anaerobic ammonium oxidation,anammox)工艺被认为是当前污水生物脱氮领域最经济的处理工艺,有利于实现污水处理厂的能源自给。厌氧氨氧化菌是该工艺的核心功能微生物。以厌氧氨氧化菌为主导微生物形成的厌氧氨氧化颗粒污泥具有沉速大、污泥持留能力强及对不利环境抵抗能力强等突出优势,是实现厌氧氨氧化工艺最有前景的污泥形态。本论文围绕厌氧氨氧化颗粒,介绍了厌氧氨氧化菌的特性、种类及代谢途径,综述了厌氧氨氧化颗粒污泥的形成假说及与厌氧氨氧化颗粒污泥聚集密切相关的胞外聚合物(extracellular polymeric substance,EPS)和群体感应研究现状,并对今后厌氧氨氧化颗粒的研究进行了展望,以期为后续厌氧氨氧化颗粒的研究及厌氧氨氧化颗粒工艺的优化提供参考。     

污水处理厂污泥膨胀和污泥发泡的比较分析

活性污泥法由于操作简单、处理效果好被广泛应用于市政污水和工业废水的处理。污泥膨胀和污泥发泡现象影响二次沉淀池的泥水分离过程和生物反应池的微生物量稳定,严重困扰着污水处理厂的正常运行,被称为污水处理厂的"癌症"。本文从污泥膨胀和污泥发泡的定义及分类出发,全面地比较了表征污泥膨胀和污泥发泡的方法、引起污泥膨胀和污泥发泡的丝状细菌种类及控制污泥膨胀和污泥发泡方法的异同,并探讨了污泥膨胀和污泥发泡问题的未来研究方向和控制策略,期望能够为今后污泥膨胀和污泥发泡问题的研究和调控提供有价值的参考。     

微生物技术在医疗废水处理中的应用

医院污水含有多种病菌、病毒及寄生虫,其直接危害和潜在危害都是显而易见的,因此,进行医疗废水治理,已成为当务之急。微生物处理主要是通过采用活性污泥法、生物接触氧化法、膜生物反应器、曝气生物滤池法等对污水进行处理,从而有效去除水中的有机物,破坏病原微生物赖以生存的物质基础和保障消毒效果。不同的处理工艺各有优缺,适合于不同规模的医院。     

污水处理厂污泥处理技术的探讨

近年来,随着社会工业的发展、技术的进步,国民生产总值日益提高。污泥污染问题也逐渐进入人们视线。本文通过对污水处理厂进水水量特征描述,重点探讨污泥处理在我国发展的现状、污水处理厂在污泥处理工程中存在的问题。在此基础上,对污水处理厂污泥处理未来发展趋势展望,提出对于污泥处理技术行之有效的建设性建议。     

荧光定量PCR监测五氯酚对好氧颗粒污泥和活性污泥中氨氧化细菌数量的影响

通过特异引物扩增环境中氨氧化细菌16S rDNAV2保守区域,将该片段克隆到T-easy载体上,PCR产物经测序和定量PCR扩增体系鉴定,证实PCR扩增产物为氨氧化细菌16S rDNA保守序列,以含该序列的重组质粒作为定量PCR监测氨氧化细菌数量的DNA标准品。用荧光定量PCR技术比较了五氯酚(PCP)对好氧颗粒污泥和活性污泥中氨氧化细菌数量的影响。结果表明,不加PCP的反应器中,好氧颗粒污泥和活性污泥中氨氧化细菌的数量分别为4.28×107±5.44×106cells/(g干污泥)和2.51×109±8.61×108cells/(g干污泥)。随着PCP浓度的增加(0~50mg/L),PCP对氨氧化细菌数量的影响不大(P>0.05),而且,污泥中氨氧化细菌的数量与氨氮的去除率无直接的正相关关系(P>0.05),PCP主要是抑制氨氧化细菌的代谢活性导致污泥氨氮去除效率降低。     

剩余污泥资源化利用新工艺研究进展

随着城市化进程加速, 污水处理厂剩余污泥大量产生, 如何对其进行处理并有效资源化利用成为广泛关注的问题。文章在综述我国城市污水处理厂剩余污泥特征、相应处理与综合利用方法的基础上, 进一步综述了污泥干化芦苇床、人工湿地、微生物燃料电池以及相关组合工艺等剩余污泥资源化利用新工艺。总结了各种新工艺的优势以及当前尚未解决的关键问题, 对未来新工艺的潜在应用进行了展望, 以期开发出低能耗、低成本、高效率、绿色生态的技术, 真正实现剩余污泥的减量化、无害化、稳定化和资源化。     

The performance of peat-filled subsurface flow filters treating landfill leachate and municipal wastewater

The main objective of this study was to determine the treatment capacity of well-mineralized peat in vertical and horizontal flow filters designed to reduce phosphorus, nitrogen and organic matter in municipal wastewater from the town of Tapa and landfill leachate in Väätsa, Estonia. Two identically designed onsite experiments were conducted using the following filter systems: (a) a vertical flow (VF) peat filter, (b) a vertical flow peat/ash sediment filter (both materials in equal volumes) followed by a horizontal flow (HF) peat filter. Sphagnum peat and hydrated oil-shale ash (ash sediment) was used. In our experiments, one treated municipal wastewater over 6 months and another treated landfill leachate over 12 months. In both cases, effluent from a conventional treatment (aerated activated sludge treatment) plant was used. The median value of total phosphorus (TP) concentration in Väätsa landfill leachate was 3.4 mg P L^?1 and in municipal wastewater from Tapa 4.9 mg P L^?1. The reduction of TP in VF peat filters during the first 6 months was 58% and 63%, and in peat/ash sediment filters 94% and 67% for the Tapa experiment and the Väätsa experiment, respectively. Both experiments demonstrated that the P-removal efficiency in VF peat filters begins to decrease after 6 months of operation. The purification efficiency in HF filters fluctuated, and no significant removal of TP was found. In the removal of organic matter (BOD, COD values) and nitrogen, the best results were obtained in VF peat filters.     

猪场恶臭的生物技术综合处理

集约化猪场恶臭的生物处理可以在饲养的营养技术、饲养过程和粪便处理阶段分别处理,试验表明使用含有微生物制剂等成分的除臭剂为饲料添加剂,可使猪舍氨气和硫化氧分别降低38．6％和20．6％,调节池中氨气和硫化氧分别降低14．7％和20．4％,臭气浓度降低43.8％。而在猪舍和饲养过程中使用恶臭吸附剂直接放置于猪场环境中,可降低猪舍中的氨气和硫化氢浓度29．5％和30．4％,降低调节池中的氨气和硫化氢30．2％和0％,降低臭气浓度31．9％。在猪场污水处胛阶段使用雾化除臭处理设备,可以降低调节池、贮粪池和水力筛池的氨气浓度14．7％、24．6％和48.2％,分别降低硫化氢浓度18．1％、25．8％和13．0％,同时降低猪场臭气浓度82．6％。     

Identifying an interfering factor on chemical oxygen demand (COD) determination in piggery wastewater and eliminating the factor by an indigenous Pseudomonas stutzeri strain

AIMS: This study attempted to demonstrate nitrite interference on chemical oxygen demand (COD) determination in piggery wastewater, and the capability of aerobic denitrification of the SU2 strain which is capable of promoting the efficiency of nitrogen and COD removal from piggery wastewater. METHODS AND RESULTS: This study was performed in a 17-litre reactor with a 30% packing ratio, with a ratio of immobilized SU2 cells to sludge of 100:1. The ratio of aeration to nonaeration was 4 : 1.5. Removal efficiency of COD was 86.8%. Removal efficiency of BOD and SS was higher than 90%, and removal efficiency of NH4+-N and TKN was almost 100%. CONCLUSIONS: NO2- -N interference is significant when its concentration in piggery wastewater exceeds 100 mg l-1. COD in piggery wastewater can be indirectly reduced following nitrite reduction by SU2 strain. SIGNIFICANCE AND IMPACT OF THE STUDY: Utilizing immobilized SU2 cells in coordination with an SBR system simultaneously reduces nitrite and COD concentrations.     

Modeling the system dynamics for nutrient removal in an innovative septic tank media filter

A next generation septic tank media filter to replace or enhance the current on-site wastewater treatment drainfields was proposed in this study. Unit operation with known treatment efficiencies, flow pattern identification, and system dynamics modeling was cohesively concatenated in order to prove the concept of a newly developed media filter. A multicompartmental model addressing system dynamics and feedbacks based on our assumed microbiological processes accounting for aerobic, anoxic, and anaerobic conditions in the media filter was constructed and calibrated with the aid of in situ measurements and the understanding of the flow patterns. Such a calibrated system dynamics model was then applied for a sensitivity analysis under changing inflow conditions based on the rates of nitrification and denitrification characterized through the field-scale testing. This advancement may contribute to design such a drainfield media filter in household septic tank systems in the future.     

Application of chemical precipitation and membrane bioreactor hybrid process for piggery wastewater treatment

This study was conducted to investigate the chemical precipitation (CP) and membrane bioreactor (MBR) hybrid process for the treatment of piggery wastewater. Average removal efficiencies for BOD, COD and turbidity in CP process were 64.3%, 77.3% and 96.4%, respectively. CP process had a moderate effect on NH₃–N removal (40.4%) which improved up to 98.2% mainly due to nitrification and filtration processes in MBR. The average removal efficiencies of BOD, COD and turbidity in MBR were 99.5%, 99.4% and 99.8%, respectively. Monod equation was used to explain the microbial activities in terms of specific growth rate. The specific growth rate of bacteria in aeration tank (N-batch) and anoxic tank (D-batch) were 0.013 and 0.005 d^?1 with a biomass yield of 0.78 and 0.43 mg MLSS produced/mg COD utilized, respectively. Microorganisms from the N-batch and D-batch showed a low-level of nitrifying and moderate-level of denitrifying capabilities which were 1.08 mg NH₃–N/(g MLVSS.h) and 2.82 mg NO₃–N/(g MLVSS.h), respectively. Carbohydrates were the main component in extracellular polymeric substance (EPS) compounds that could be attached to the membrane surface easily and led to membrane biofouling. The increase of MLSS, EPS and sludge viscosity concentration, decrease of sludge floc size and incomplete chemical cleaning procedure resulted in the increase of membrane resistance. Total membrane resistance increased from 3.19 × 10¹² m^?1 to 5.43 × 10¹⁴ m^?1.     

Nitrogen removal from animal waste treatment water by anammox enrichment

The aim of this work was to examine the applicability of the anaerobic ammonium oxidation (anammox) process to three kinds of low BOD/N ratio wastewaters from animal waste treatment processes in batch mode. A rapid decrease of NO(2)(-) and NH(4)(+) was observed during incubation with wastewaters from AS and UASB/trickling filter and their corresponding control artificial wastewaters. This nitrogen removal resulted from the anammox reaction, because the ratio of removed NO(2)(-) and NH(4)(+) was close to the theoretical ratio of the anammox reaction. Comparison of the inorganic nitrogen removal rate of the actual wastewater and that of control artificial wastewater showed that these two kinds of wastewater were very suitable for anammox treatment. Incubation with wastewater from RW did not show a clear anammox reaction; however, diluting it by half enabled the reaction, suggesting the presence of an inhibitory factor. This study showed that the three kinds of wastewater from animal waste treatment processes were suitable for anammox treatment.     

Autotrophic denitrification and chemical phosphate removal of agro-industrial wastewater by filtration with granular medium

A novel granular medium consisting (1.5-5 mm in diameter) of inert perlite particles as nuclei and an effective surface layer containing sulfur, CaCO3 and Mg(OH)2 was developed for advanced treatment of agro-industrial wastewater. The performance of the medium was examined with a laboratory-scale down-flow fixed-bed column reactor using piggery wastewater, which had been treated by an upflow anaerobic sludge blanket reactor and a trickling filter. The removal efficiency of NOx- -N was more than 70% with a NOx- -N loading rate of less than approximately 0.3 kg Nm(-3) d(-1); the removal efficiency dropped due to the accumulation of nitrite when the loading rate exceeded that value. A significant drop of phosphate and Mg2+ concentrations occurred when the effluent pH exceeded 7.9. Ammonium was removed with an average removal efficiency of 12.4%. These results indicated that the crystalline reaction of PO4(3-), Mg2+ and NH4+ (MAP reaction) under alkaline conditions contributed to the removal of phosphate. This medium could be useful for the simultaneous reduction of nitrogenous and phosphorus compounds in biologically treated agro-industrial wastewater.     

Treatment of recycled wastewaters from fishmeal factory by an anaerobic filter

Fishmeal industries processes produce effluents with high load organic matter. These effluents, after recycling and physical-chemical pretreatment, have a high organic content (5-6 g COD/l), proteins (3-5 g/l), salinity close to sea water, sodium chloride (30 g/l) and sulphate (1-3.3 g/l). An anaerobic filter was used for the treatment of this wastewater, with marine sediment as anaerobic inoculum. Anaerobic filter removed up to 70% of the influent COD concentrations at organic loading rates (OLR) of 9.5 and 14.3 (g/l d) and sulphate up to 80% at OLR of 7.1 and 14.3 (g/l d) whereas the pH ranged between 7.0 and 7.5. These results show that anaerobic filter systems are applicable to recycled wastewaters from fishmeal.     

Modelling of biological processes during aerobic treatment of piggery wastewater aiming at process optimisation

A dynamic mathematical model was developed for the simulation of the aerobic treatment of piggery wastewater. This model includes the carbon oxidation, the nitrification and the denitrification. According to the experimental results obtained during this study, a modified version of the activated sludge model No. 1 has been developed. The model includes (1) nitrite as intermediate of nitrification and denitrification, (2) the distinction between the anoxic heterotrophic yield and the aerobic heterotrophic yield, respectively equal to 0.53 and 0.6 and (3) the first-order hydrolysis of the slowly biodegradable fraction. The calibration and the validation of the model was performed using experimental data from three experiments with two piggery wastewaters. A set of kinetic and stoichiometric parameters emerged from these tests. Except the kinetic of hydrolysis of the slowly biodegradable organic matter varying from 6 to 25 gCOD(gCODday)(-1), all other parameters were similar for all experiments. The dissolved oxygen concentration was identified as the main variable influencing the nitrite accumulation during nitrification. In the calibrated model, the oxygen half-saturation coefficient of the ammonium oxidisers (0.3g O(2)m(-3)) was lower than for the nitrite oxidisers (1.1 gO(2)m(-3)), leading to nitrite accumulation when the dissolved oxygen concentration was low. Simulations with the proposed model could be very useful for improved design and management of biological treatment of piggery wastewaters, particularly in case of partial nitrification to nitrite directly followed by denitrification.