干湿交替运行对地下渗滤系统脱氮效果的影响

利用室内模拟系统,在进水铵氮(NH4+-N)浓度30～37.5mg·L-1、水力负荷0.08m3.m-2.d-1的条件下,考察了干湿交替运行对污水地下渗滤系统脱氮效果的影响,分析了干湿比对基质理化性质、脱氮微生物数量以及基质氧化还原电位(ORP)变化的影响。结果表明,基质渗透率和硝化细菌的数量随干湿比的增加而增加,反硝化细菌的数量则随干湿比的增加而减少,比容积和氨化细菌的数量受干湿比的影响较小,各深度基质层ORP均随干湿交替运行而高低起伏。推荐地下渗滤系统启动期的干湿比3∶1,启动周期为20d;稳定运行期干湿比1∶1,NH4+-N及TN的去除率可分别达到86.9%和79.1%,同时,有机污染物去除效果好,出水水质满足再生利用-景观环境用水水质标准(GB/T18921—2002)。     

地下渗滤系统处理生活污水的技术难点及对策

以土地处理系统为代表的污水自然处理技术,遵循循环再生、和谐共存、整体优化、区域分异等原理,不仅对各种污染物有极高的去除效率,并可实现污水的处理与利用相结合。本文介绍了地下渗滤系统的工艺原理、技术特征,并阐述了国内外研究的最新进展,讨论了应用中的主要技术难点和解决途径,包括选配基质、缓解土壤堵塞以及提高系统氮的去除效果和水力负荷的方法等,指出地下渗滤系统应在强化预处理的基础上,采用合理调配土壤组成以提高水力负荷的运行方式。     

生物膜型污水脱氮系统中膜结构及微生物生态研究进展

生物膜法污水脱氮系统主要利用生物膜中脱氮功能微生物的代谢活动去除氮素,从而达到净化水质的目的,研究脱氮生物膜的微观结构和微生物生态是揭示生物膜脱氮机理从而提高脱氮效率的重要途径.本文综述了生物膜型污水脱氮系统类型、生物膜微观结构特征及其影响因素、生物膜型污水脱氮系统内氮素传质过程、脱氮机理和生物膜数学模型等方面的研究进展.另外,本文介绍了生物膜型污水脱氮系统内生物膜脱氮功能微生物分布特征,不同生物膜脱氮系统、底物、运行条件和时间对功能微生物群落影响,及新型脱氮功能微生物等方面的研究进展,为生物膜脱氮技术的深入研究提供参考.     

反硝化细菌在污水脱氮中的作用

反硝化是在反硝化细菌的作用下,以硝酸盐作为最终电子受体而进行的无氧呼吸过程。从污水脱氮的角度论述反硝化在污水脱氮中的作用、污水脱氮的机理、污水脱氮过程中反硝化作用的影响因素等。从反硝化的角度出发,论述了反硝化细菌的类群、反硝化作用的机理、反硝化细菌细胞中参与反硝化过程的关键酶。另外,还论述了近年来发现的有氧反硝化细菌、自养反硝化细菌及反硝化除磷细菌等方面的研究进展。     

新型脱氮微生物与水体脱氮新工艺研究进展

氨氮是河流等淡水资源有机污染的主要污染指标之一。生物脱氮具有低成本、高效、无二次污染和易操作等优点,极具发展前景。重点概述了水体净化系统中新型脱氮微生物的种类及研究进展,介绍了厌氧氨氧化、短程硝化-反硝化和分段进水生物脱氮等高效节能新工艺的工艺原理。     

普通小球藻对养殖污水脱氮除磷的效果研究

随着我国养殖业的不断发展,养殖污水排放量的日益增加,养殖污水的高氮、磷含量导致水体富营养化问题日趋严重。小球藻是光能自养生物,能有效同化氮、磷,使污水中的氮、磷减少。本研究通过在实验室模拟不同氮、磷含量的养殖污水环境,分析小球藻对氮、磷的去除效果;在此基础上,用小球藻处理某养殖场污水;并联合膨润土与小球藻,探究两者脱氮除磷的协同作用能力及膨润土对小球藻细胞沉降的效果。结果表明,小球藻对模拟污水的氨氮去除率可达80%,对磷酸根的最高去除率接近100%;对养殖污水中的氮、磷也有一定的去除效果;但养殖污水成分复杂,小球藻的生长被抑制。膨润土与小球藻的结合,能够提高污水中的氮磷去除率并帮助藻细胞快速沉降,为污水处理后藻细胞的收集处理提供了有效方法。     

污水脱氮功能微生物的组学研究进展

生物脱氮是污水处理厂的核心,掌握生物脱氮过程相关微生物代谢特性,对于探索微生物资源和提高污水处理厂脱氮性能具有重要意义。近年来,分子生物学方法不断发展和改进,已被广泛应用于揭示脱氮微生物群落多样性、组成结构和潜在功能等方面,大幅提升了研究者们对污水生物脱氮系统中微生物,尤其是不可培养微生物的代谢机理、抑制调控原理及新型生物脱氮工艺途径的认识。本文对流行的分子生物学方法(16S rRNA基因测序、实时荧光定量PCR技术、宏基因组学、宏转录组学、宏蛋白质组学和代谢组学)进行了介绍,综述了其在硝化细菌、反硝化细菌、完全氨氧化细菌、厌氧氨氧化细菌、厌氧铁氨氧化细菌、硫酸盐型厌氧氨氧化细菌及亚硝酸盐/硝酸盐型厌氧甲烷氧化微生物等方面的研究进展,阐明了这些氮素转化微生物在氮循环过程的代谢途径和酶促反应,并从标准测定方法构建、不同方法的联用及跨学科结合和检测方法的简易化这3个方面展望了分子生物学方法的技术突破及其在污水生物处理系统中的应用前景。本综述从系统角度全面认识脱氮微生物群落及其结构,为未来污水处理生物脱氮微生物的研究提供了新方向。     

湖泊氮素氧化及脱氮过程研究进展

自然界中氮的生物地球化学循环主要由微生物驱动,由固氮作用、硝化作用、反硝化作用和氨化作用来完成。过去数十年间,随着异养硝化、厌氧氨氧化和古菌氨氧化作用的发现,人们对环境中氮素循环认识逐步深入,提出了多种脱氮途径新假说。对湖泊生态系统中氮素的输入、输出及其在水体、沉积物和水土界面的迁移转化过程进行了概括,对湖泊生态系统中反硝化和厌氧氨氧化脱氮机理及脱氮效率的最新研究进展进行了探讨,并对以后的氮素循环研究进行了展望。     

脱氮微生物及脱氮工艺研究进展

脱氮是大部分污水处理系统中不可缺少的一环。由于具有经济高效、工艺简单和无二次污染等显著优势,生物脱氮工艺在最近数十年中备受关注。根据脱氮微生物的生理特性和脱氮机制不同,文中分类综述了近年来生物脱氮工艺的研究进展,重点对比分析了硝化菌、反硝化菌和厌氧氨氧化菌以及以这些菌为基础的不同生物脱氮工艺的优缺点,为复杂污水环境的脱氮工艺选择提供参考。基于微生物脱氮机制,通过合成生物学技术开发高效脱氮菌株,结合不同工艺优点并应用自动化模拟最佳条件,从而建立经济高效的脱氮工艺将是未来发展的重要方向。     

Effects of hydraulic loading rate on pollutants removal by a deep subsurface wastewater infiltration system

The subsurface wastewater infiltration (SWI) system proved to be an effective and low-cost technique for decentralized sewage treatment in areas without adequate domestic treatment facilities. Field-scale experiments were conducted through a deep SWI system, with effective depth of 1.5 m, under hydraulic loading rates of 0.040, 0.065, 0.081 and 0.10 m³/m² d. Taking the hydraulic and treatment efficiencies into consideration, the hydraulic loading rate of 0.081 m³/m² d was recommended. Under this condition, NH₃-N, TN, and COD removal efficiencies were 86.2 ± 3.0, 80.7 ± 1.9 and 84.8 ± 2.1%, respectively. In the effluent, NH₃-N concentration declined to 2.3-4.4 mg/L, accounting for 63.2-65.6% of TN. NO₃-N concentration increased from 0.2 to 0.3 mg/L in the influent to 2.0-2.5 mg/L in the effluent. The nitrifying bacteria number declined with increased depth, while the amount of denitrifying bacteria increased. The analysis of results about the nitrifying and denitrifying bacteria distribution indicated that the most effective ranges for nitrification and denitrification process were 0.3-0.7 m and 0.7-1.5 m, respectively.     

Operation and modeling of bench-scale SBR for simultaneous removal of nitrogen and phosphorus using real wastewater

Experimental work was carried out on nitrogen and phosphorus removal from real wastewater using a bench-scale SBR process. The phosphorus removal was stable and the phosphorus concentration remaining in the reactor was maintained within 1.5 ppm, regard-less of the addition of an external carbon source. In the case of nitrogen, an external carbon source was necessary for denitrification. The effect on denitrification with the addition of various carbon sources, such as glucose, methanol, acetate, and propionate, was also investigated. Acetate was found to be the most effective among those tested in this study. When 100 ppm (theoretical oxygen demand) of sodium acetate was added, the average rate of denitrifiaction was 2.73 mg NO₃⁻-N (g MLSS)⁻¹ h⁻¹, which wasca. 4 times higher than that with the addition of 200 ppm of methanol. The phosphorus and nitrogen concentrations were both maintained within 1.5 ppm by the addition of an appropriate amount of a carbon source during a long-term operation of the SBR. The mathematical modeling was performed using Monod kinetics, other microbial kinetics, mass balances, and stoichiometry. The modeling was found to be useful for predicting the SBR operation and optimizing the HRT.     

潜流人工湿地在城市污水三级处理中的应用

采用页岩/钢渣强化潜流人工湿地作为城市污水处理厂三级处理工艺.结果表明:在平均水力负荷为0.32 m·d-1的条件下,当进水有机物(CODcr)、总氮(TN)、总磷(TP)平均浓度为33.9、15.1和1.57 mg·L-1时,出水CODcr平均浓度为13.6 mg·L-1去除率为60%,面积速率常数KA值为0.3 m·d-1温度对CODcr的去除影响不明显;出水TN浓度在5.4～14.3 mg·L-1之间波动,KA值为0.09～0.31 m·d-1,去除率受温度的影响较大,随着进水硝态氮比例的提高和运行时间的延长,湿地对TN的去除效率有上升趋势;稳定阶段出水TP浓度为0.6 mg·L-1去除率为50%,KA为0.26 m·d-1温度对,TP去除影响不大.     

Effect of influent COD/N ratio on biological nitrogen removal (BNR) from high-strength ammonium industrial wastewater

The effect of influent COD/N ratio on biological nitrogen removal (BNR) from high-strength ammonium industrial wastewater was investigated. Experiments were conducted in a modified Ludzack–Ettinger pilot-plant configuration for 365 days. Total nitrification of an influent concentration of 1200 mg NH₄⁺–N l⁻¹ was obtained in this period. Influent COD/N ratios between 0.71 and 3.4 g COD g N⁻¹ were tested by varying the nitrogen loading rate (NLR) supplied to the pilot plant. An exponential decrease of nitrification rate was observed when the influent COD/N ratio increased.

The experimental COD/N ratio for denitrification was 7.1±0.8 g COD g N⁻¹ while the stoichiometric ratio was 4.2 g COD g N⁻¹. This difference is attributable to the oxidation of organic matter in the anoxic reactor with the oxygen of the internal recycle. The influence of influent COD/N ratio on the treatment of high-strength ammonium industrial wastewater can be quantified with these results. The influence of COD/N ratio should be one of the main parameters in the design of biological nitrogen removal processes in industrial wastewater treatment.     

Simultaneous removal of carbon and nitrogen from municipal-type synthetic wastewater using net-like rotating biological contactor (NRBC)

The treatment of municipal-type synthetic wastewater was carried out using a three stages net-like rotating biological contactor (NRBC). The results indicated that, compared with conventional rotating biological contactor (RBC), NRBC have several advantages, such as quick start-up, high biomass concentration and can handle high organic loading rates. The COD and total nitrogen removal rates achieved were 78.8–89.7% and 40.2–61.4%, respectively, in aerobic treatment of low COD municipal-type wastewater at hydraulic retention times (HRT) from 5 to 9 h. The COD removal rate achieved 80–95% when organic loading varied between 16 and 40 gCOD/m² d. A large amount of nematodes were found in the NRBC system, which made the NRBC system produce relatively low amounts of waste sludge, due to their grazing.     

Role of heterotrophic nitrifiers and aerobic denitrifiers in simultaneous nitrification and denitrification process: a nonconventional nitrogen removal pathway in wastewater treatment

Bacterial species capable of performing both nitrification and denitrification in a single vessel under similar conditions have gained significance in the wastewater treatment scenario considering their unique character of performing the above reactions under heterotrophic and aerobic conditions respectively. Such a novel strategy often referred to as simultaneous nitrification and denitrification (SND) has a tremendous potential in dealing with various wastewaters having low C : N content, considering that the process needs very little or no external carbon source and oxygen supply thus adding to its cost-effective and environmentally friendly nature. Though like other micro-organisms, heterotrophic nitrifiers and aerobic denitrifiers convert inorganic or organic nitrogen-containing substances into harmless dinitrogen gas in the wastewater, their ecophysiological role in the global nitrogen cycle is still not fully understood. Attempts to highlight the role played by the heterotrophic nitrifiers and aerobic denitrifiers in dealing with nitrogen pollution under various environmental operating conditions will help in developing a mechanistic understanding of the SND process to address the issues faced by the traditional methods of aerobic autotrophic nitrification–anaerobic heterotrophic denitrification.     

生物反应器填埋场系统渗滤液的脱氮性能

利用填埋场垂直分布的好氧-缺氧-厌氧的独特生态环境,并采用填埋垃圾上层间歇曝气充氧的方式,研究了生物反应器填埋场系统渗滤液的脱N性能.结果表明,填埋垃圾上层间歇曝气充氧,促进了填埋垃圾层硝化细菌和反硝化细菌的生长,且可使反硝化细菌的数量比普通的填埋垃圾层高4～13个数量级,硝化细菌的最大数量可达到10⁹个·g^-1;营建了填埋场内硝化、反硝化等脱N反应的生物环境,有利于回流渗滤液含N化合物的去除.试验结束时,其渗滤液NH₄⁺-N和TN浓度分别为186和289 mg·L^-1,仅为对照的18%和26％.此外,填埋垃圾上层间歇曝气充氧也有利于填埋垃圾的降解,提高垃圾的稳定化效果.     

浮床黑麦草对城市生活污水氮循环细菌繁衍和脱氮效果的影响

通过设施大棚内容积为1.5m3的人工模拟池试验,研究了浮床黑麦草对模拟城市生活污水氮循环细菌繁衍和脱氮效果的影响。通过研究,阐明浮床植物去除污染水体氮素的可能途径。研究结果表明:浮床黑麦草对模拟城市生活污水总氮和氨氮的去除效果分别达到了31.6%和43.0%;浮床黑麦草根际和根系正下方是各类氮循环细菌生长的最佳区域;浮床黑麦草处理有效地提高了系统氮循环细菌的数量,16d的试验结束时细菌总数(A,单位为CFU.mL-1)达到最大值,其lg(A/(CFU.mL-1))增加至8.82,各类氮循环细菌比对照高3-5个数量级;同时,浮床黑麦草处理显著提高了氮循环细菌的群落多样性,系统内氨化菌、硝化菌、亚硝化菌和反硝化菌共存;明确了浮床黑麦草的吸收同化和氮循环细菌的生物脱氮是浮床黑麦草净化水质的两个重要途径。