STUDIES ON THE PURIFICATION AND RECLAMATION OF WASTE-WATER FROM A MEDIUM-SIZED CITY BY AN INTEGRATED BIOLOGICAL POND SYSTEM

The feasibility of an inexpensive wastewater treatment system is evaluated in this study. An integrated biological pond system was operated for more than 3 years to purify the wastewater from a medium-sized city, Central China. The experiment was conducted in 3 phases with different treatment combinations for testing their purification efficiencies. The pond system was divided into 3 functional regions: influent purification, effluent upgrading and multi-utilization. These regions were further divided into several zones and subzones. Various kinds of aquatic organisms, including macrophytes, algae, microorganisms and zooplankton, were effectively cooperating in the wastewater treatment in this system. The system attained high reductions of BOD5, COD, TSS, TN, TP and other pollutants. The purification efficiencies of this system were higher than those of most traditional oxidation ponds or ordinary macrophyte ponds. The mutagenic effect and numbers of bacteria and viruses declined significantly during the process of purification. After the wastewater flowed through the upgrading zone, the concentrations of pollutants and algae evidently decreased. Plant harvesting did not yield dramatic effects on reductions of the main pollutants, though it did significantly affect the biomass productivity of the macrophytes. The effluent from this system could be utilized in irrigation and aquaculture. Some aquatic products were harvested from this system and some biomass was utilized for food, fertilizer, fodder and some other uses. The wastewater was reclaimed for various purposes.

生物质煤气废水氨氮脱除的研究

生物质煤气废水是一种新出现的高浓度氨氮有机废水。作者采用化学沉淀法去除该废水中的氨氮，研究了不同沉淀剂、pH、温度和搅拌时间对氨氮去除效果的影响。结果表明，MgCl2＋Na3PO4·12H2O明显优于其他沉淀剂组合。当n（Mg^2＋）：n（NH4^＋）：n（PO4^3-）=1：1：1、pH10．0、温度30℃、搅拌时间30min时，废水中的氨氮质量浓度从处理前的222mg/L降到17mg／L，去除率为92.3％。

Design and Operation of A 5.5 MWe Biomass Integrated Gasification Combined Cycle Demonstration Plant

The design and operation of a 5.5 MWe biomass integrated gasification combined cycle (IGCC) demonstration plant, which is located in Xinghua, Jiangsu Province of China, are introduced. It is the largest complete biomass gasification power plant that uses rice husk and other agricultural wastes as fuel in Asia. It mainly consists of a 20 MWt atmospheric circulating fluidized-bed gasifier, a gas-purifying system, 10 sets of 450 kW(e) gas engines, a waste heat boiler, a 1.5 MWe steam turbine, a wastewater treatment system, etc. The demonstration plant has been operating since the end of 2005, and its overall efficiency reaches 26-28%. Its capital cost is less than 1200 USD/kW, and its running cost is about 0.079 USD/kWh based on the biomass price of 35.7 USD/ton. There is a 20% increment on capital cost and 35% decrease on the fuel consumption compared to that of a 1 MW system without a combined cycle. Because only part of the project has been performed, many of the tests still remain and, accordingly, must be reported at a later opportunity.

Establishment and characterization of dual-species biofilms formed between a 3,5-dinitrobenzoic-degrading strain and bacteria with high biofilm-forming capabilities

In this study, the possibility of establishing a dual-species biofilm from a bacterium with a high biofilm-forming capability and a 3,5-dinitrobenzoic acid (3,5-DNBA)-degrading bacterium, Comamonas testosteroni A3, was investigated. Our results showed that the combinations of strain A3 with each of five strains with a high biofilm-forming capability (Pseudomonas sp. M8, Pseudomonas putida M9, Bacillus cereus M19, Pseudomonas plecoglossicida M21 and Aeromonas hydrophila M22) presented different levels of enhancement regarding biofilm-forming capability. Among these culture combinations, the 24-h dual-species biofilms established by C. testosteroni A3 with P. putida M9 and A. hydrophila M22 showed the strongest resistance to 3,5-DNBA shock loading, as demonstrated by six successive replacements with DMM2 synthetic wastewater. The degradation rates of 3,5-DNBA by these two culture combinations reached 63.3-91.6% and 70.7-89.4%, respectively, within 6 h of every replacement. Using the gfp-tagged strain M22 and confocal laser scanning microscopy, the immobilization of A3 cells in the dual-species biofilm was confirmed. We thus demonstrated that, during wastewater treatment processes, it is possible to immobilize degrader bacteria with bacteria with a high biofilm-forming capability and to enable them to develop into the mixed microbial flora. This may be a simple and economical method that represents a novel strategy for effective bioaugmentation.

UASB反应器处理维生素C生产废水研究

维生素C生产废水有机物浓度高、成分复杂、排放量大，是一种亟待处理的典型工业废水。本研究分别采用实验室规模和中试规模的升流式厌氧颗粒污泥床反应器（UASB）对该制药工业废水的厌氧生物处理工艺进行了较为深入的研究。同时采用两种不依赖于纯培养的分子生物学手段—变性梯度凝胶电泳（DGGE）和扩增核糖体DNA限制性分析（ARDRA）技术揭示了UASB反应器不同运行阶段污泥中微生物群落多样性组成及变化。此外，首次研究了零价铁（Fe0）在厌氧消化过程中对反应器运行及微生物群落结构的影响。 采用城市污水处理厂厌氧消化池絮状污泥和处理啤酒废水的颗粒污泥混合接种，小试中温（35±1℃）UASB反应器在其运行的第65天启动成功。反应器稳定运行阶段，在进水COD浓度为9000mg/L、水力停留时间为12h、容积负荷为13.6 kgCOD/m3.d条件下，其COD去除率稳定在85~90%之间，沼气产率达到4.5 m3/m3.d，沼气甲烷含量平均为72%。中试UASB反应器的接种污泥为厌氧消化污泥，其启动时间相对较长，为90天。在稳定运行期，反应器的进水COD浓度为8000~10000mg/L，水力停留时间和容积负荷分别保持在12~16h和10.6~14.2 kgCOD/m3.d范围，该阶段反应器的平均COD去除率稳定在85%左右，沼气产率平均为5.2m3/m3.d，沼气中甲烷含量为69%。上述结果表明中温UASB工艺用于维生素C生产废水处理是高效、可行的。 与对照反应器相比，添加Fe0的小试UASB反应器的COD去除率和沼气产量分别提高了6.5%和10.2%。同时，磷酸盐平均去除率为79%，比对照提高了64%，目前尚未见类似研究报道。在中试规模的UASB反应器中补充一定量的Fe0可缩短反应器启动时间，促进颗粒污泥的形成，该结果可能具有重要的应用价值。培养试验进一步表明，Fe0可以作为产甲烷菌还原CO2生成甲烷的电子供体。培养实验还表明，当系统中存在硝酸盐（0.40 mM）和硫酸盐（0.26 mM）时，Fe0促产甲烷过程受到一定程度的抑制。 采用细菌通用引物968F/1401R和341F/907R获得的PCR-DGGE指纹图谱均表明UASB反应器不同运行阶段细菌种群结构变化明显。小试和中试稳定期污泥的微生物多样性均高于各自初始接种污泥。产甲烷菌通用引物340F/519R的PCR-DGGE结果显示，虽然接种污泥中产甲烷菌的丰富度系数略低于稳定期，但总体而言，反应器运行期间产甲烷菌的种群组成相对稳定。 通过构建不同处理和不同运行阶段污泥样品的16S rRNA基因文库并对克隆基因进行限制性内切酶消化、测序分析。结果表明，稳定期两个反应器微生物群落结构相似，但与各自接种污泥差异明显。小试UASB反应器接种污泥中细菌的优势菌群分别为变形菌纲的δ亚纲（28.7%）和β亚纲（17.4%），至稳定运行期则演替为革兰氏阳性低GC菌群（21.9%）和变形菌纲的δ亚纲（14.0%）。中试反应器接种污泥Green non-sulfer bacteria（25.9%）和变形菌纲的δ亚纲（16.4%）类群占优势，而稳定期Green non-sulfer bacteria类群（17.9%）、革兰氏阳性低GC菌群（16.2%）和变形菌纲的δ亚纲（15.4%）为优势菌群。 产甲烷菌的优势克隆为SRJ 230、SRJ 26和SRJ 583，前两者分别与Methanosaeta concilii和未培养的Methanobacteria-like克隆Gran7M4的同源性达到97%和98%，后者与Methanomethylovorans. sp同源性为99%。接种污泥中上述类群占总克隆数量的比例较低。小试、中试接种污泥中产甲烷菌分别占7.8%和3.0%，但稳定运行期，该比例明显增加，分别达到21.9%和18.8%。上述结果表明启动期与稳定期污泥产甲烷菌种群组成相对稳定，但各类群数量明显增加。 添加Fe0的UASB反应器稳定运行期污泥中产甲烷菌比例（31.2%）高于对照反应器（24.2%）, 革兰氏阳性低GC类群、变形菌纲的δ亚纲比例差异不明显，而变形菌纲β亚纲（6.0%）和Green non-sulfer bacteria（9.2%）的比例均分别低于对照反应器（13.1%和17.1%）。该结果表明，添加Fe0使反应器内微生物群落多样性发生了显著变化。 此外，在添加Fe0的UASB反应器中检测到特异性的克隆SRJ 341和SRJ 320，两者分别同磷酸盐去除和铁氧化有关的克隆子Orbal D41和Clone195的序列相似性达95%和96%。这两个类群可能分别与磷酸盐去除及铁促产甲烷作用密切相关。这一结果尚未见报道。

污灌和农药对农田土壤假单胞菌种群的影响

随着环境污染问题的日益严重，微生物修复起到越来越重要的作用。假单胞菌是土壤微生物中最重要、研究最多的细菌之一，能降解简单和复杂的有机物，它们因此而广泛的存在于土壤和水体。但有关于石油、重金属及农药污染物对农田土壤假单胞菌多样性及种群结构的影响却缺乏全面和系统的认识。 本论文首次采用传统微生物培养方法与PCR-DGGE等现代微生物分子生态学研究方法相结合的手段，系统评价了长期含石油和重金属污水灌溉对中国最大的石油、重金属污灌区——沈抚、张士灌区农田土壤中的假单胞菌多样性及其种群结构的影响。同时，本论文也研究了乙草胺、甲胺磷对黑土假单胞菌多样性及种群结构的影响。得出以下结果： 石油污灌区土壤中总的假单胞菌多样性显著高于重金属污灌区；石油污灌区旱田土壤假单胞菌多样性接近于对照清洁土壤,同时低于相似污染程度的石油污灌区水田土壤。进一步测序发现，Pseudomonas mendocina、Pseudomonas stutzeri、Pseudomonas aeruginosa是所分析石油和重金属污灌区土壤中的优势类群，说明在长期污染胁迫下这3种假单胞菌分别得到了不同程度的富集。DGGE 结果显示石油和重金属污染土壤样品的可培养假单胞菌多样性没有显著差异，但均低于对照清洁土壤样品。对各个土壤样品可培养假单胞菌菌株进行REP-PCR基因分型，结果表明这些假单胞菌之间有显著的遗传差异。进一步测序表明，土壤样品中可培养假单胞菌优势类群中含有Pseudomonas. fluorescens 和Pseudomonas. Putida两种。 黑土农田土壤中使用乙草胺会严重降低总的及可培养假单胞菌群落的多样性，而且在5周内不能恢复。而甲胺磷处理土壤与对照相比则差异不显著，并且经过一段时间的适应，土壤中的总的及可培养假单胞菌种群不仅得到恢复而且超过对照。对各处理土壤总的及可培养假单胞菌DGGE谱带类型聚类分析，发现乙草胺、甲胺磷处理土壤样品均各自聚为一簇，说明农药污染类型是影响土壤中假单胞菌种群结构的重要因素。

污水处理体系中的微生物群落特征研究

污水生物处理系统本质上是一种人工强化的工程化微生态系统。污水处理过程往往由多个功能互补的反应单元协同完成，例如因对污水中有机碳、氮和磷兼具良好的去除功能而在城市污水处理中被广泛应用的Anoxic / Oxic（A/O）生物处理工艺。不同反应单元特有的微生物群落之间的相互关系和相互作用与处理系统的稳定性和处理效率密切相关。所以对污水处理系统中微生物群落进行系统分析非常重要。研究系统中微生物群落的时空演替对于优化处理系统的设计和操作具有重要意义。但是，以往对于污水处理系统中微生态系统的解析多数针对实验室规模的其中个别反应器独立进行，还缺乏从系统水平对实际大规模运行的整个污水处理过程中所有反应单元群落进行分析的研究。 悬挂链移动曝气系统是对A / O工艺的完善和发展。悬挂链曝气工艺的实现是依靠悬挂链移动曝气设备和完善的自动控制系统来完成的。可以在系统中实现类似多级A/O的可能性，水力停留时间较长，污泥龄达到15天以上，能够完全实现A / O 工艺。 目前正被广泛应用在各种行业的污水处理项目中。 本文应用基于细菌16S rRNA中的PCR扩增方法（Polymerase Chain Reactor），结合变性梯度凝胶电泳指纹分离技术（Denaturing Gradient Gel Electrophoresis, DGGE），对实际规模的运用Anoxic / Oxic（A/O）工艺并采用悬挂链式移动曝气技术的污水生物处理系统中微生物群落特征，主要对细菌组成结构和群落动态，细菌优势菌群的多样性以及与系统功能稳定性的关系进行了研究，拟为更全面了解活性污泥处理系统中的优势菌群特征，以及细菌群落结构和功能动态变化关系，实现对活性污泥处理的优化操作，对污染物降解功能菌群的筛选，为运用现代培养技术实现分离培养并运用于环境修复实践奠定方法和理论基础。 首先，对影响PCR-DGGE分析的重要前操作步骤进行了优化和筛选，包括两个方面：细菌基因组DNA的高效提取和纯化；不同16S rRNA靶序列对PCR-DGGE分析的影响。从中选出适合于活性污泥样品的细菌基因组DNA提取方法和PCR-DGGE分析的最优靶序列组合。 其次，运用PCR-DGGE指纹图谱技术分析了该污水处理系统中不同功能反应单元中活性污泥的细菌种群结构特征，探讨了系统运行过程中细菌种群时间和空间上的动态特征。并将图谱中所显示的优势条带进行切割回收，重复扩增，电泳检测，序列测定并与GenaBank数据库中的微生物类群进行同源性比对，探讨活性污泥中细菌种群多样性，了解污泥中可能含有的主要具有污染物降解功能的类群信息。 在整个处理过程中，同一功能反应单元中不同位置的活性污泥微生物菌群结构不同。执行不同功能的处理单元活性污泥细菌多样性和组成结构各有不同。 在系统稳定运行的状态下，细菌组成结构的时间变化动态不显著。但是在系统的不同操作条件下，主要处理池的微生物群落的DGGE遗传指纹图谱较独特。 对该处理系统污泥中优势菌群的序列测定和同源性比对表明，优势菌群所对应的细菌的16S rDNA序列可以被归属于以下四个主要的细菌系：α, β, γ- Proteobacteria 以及厚壁菌门 phylum Firmicutes （low G+C Gram-positive）。 该处理系统的优势菌群的DGGE条带拥有潜在的具有异养硝化/好氧反硝化的除 N / P 类群。该类菌群中的大多数属于Pseudomonas spp.。另外，回收到两个与已鉴定的具有异养硝化和好氧反硝化能力的Pseudomonas stutzeri 和 Pseudomonas borbori 最相似的菌株的条带。γ-变形菌纲门（γ- Proteobacteria）的微生物类群在该缺氧-好氧处理厂中分布较广泛，尤其是和 N / P 去除紧密相关的具有脱氮除磷能力的Pseudomonas 类群，而且在好氧曝气处理池中分布较广，这可能和系统中表现的好氧反硝化现象相关。 不同的操作状况下微生物群落结构有差异。增加污泥回流比，增加DO（Dissolved oxygen）浓度，COD去除率和NH4+-N去除率显著增加，总N和总P的去除率改变不显著。 最后，对整个处理过程中微生物群落结构在系统正常调控改变范围内的长期动态和稳定性进行了探讨。整个处理系统的长期稳定性与体系中的每个处理环节相关，而不是仅与其中的单个主要反应池相关。污水处理体系的功能稳定性与其中的微生物群落稳定性相关，微生物群落结构决定了生态功能，群落结构变化能反应系统的运行状况及其降解效率。

甲醇的生物降解与含甲醇废水生物处理工艺研究

甲醇作为一种有机污染物广泛存在于有机合成和石油化工等生产废水中.该研究针对氮肥生产过程中产生的低浓度甲醇废水缺乏有效回收利用工艺的现实情况，以氮肥生产过程中产生的工艺冷凝液和尿素水解水为对象，通过甲醇高效降解菌的分离、固定化，生物活性炭（BAC）反应系统的建立，小试、中试等研究工作，确定了将其回用到脱盐水系统的可行性，提出了工艺参数和工业化方案，并对BAC生物膜结构特点进行了较为深入的研究.

新型水处理剂研制及在污水处理中应用

廉价、高效、安全的新型水处理剂在水处理领域具有重要地位。针对现有絮凝剂市场中产品结构单一、产品生态安全风险较大和廉价重金属废水吸附剂的迫切需求等现状，开展新型絮凝剂和重金属吸附剂制备及在污水处理中应用研究。本文以廉价无机铝盐和玉米淀粉为原料，通过系统的小试和中试研究，优化了CAS合成配方、碱化度、合成方式、温度、时间及中间条件控制等，制备出生态安全型复合高效絮凝剂（CAS）。对模拟废水、城市生活废水和不同种类工业污水的絮凝处理结果显示：CAS具有絮凝性能高、投加量低、污泥体积小，使用后出水铝残留量低，生态安全性能高等特点。CAS综合了无机铝盐絮凝剂和天然高分子絮凝剂的优点，并在一定程度上弥补了各自组分的不足，较现有市售絮凝剂相比，絮凝效能大幅提高。Al-Ferron逐时络合比色法和扫描电镜从不同角度对CAS形态结构进行分析并对絮凝机理和生态安全机理进行了探讨。本文从污水处理角度出发，通过对模拟废水和实际工业废水的吸附处理，研究了泥炭作为亚余属吸附剂在污水处理中应用潜力，并就应用工艺的选择进行了探讨。结果表明：泥炭对受试二价重余属离子的平均吸附量高达2.05mmol／g，在6omin内丛本达到平衡。pH和共存盐浓度（如Ca~(2+)）会对泥炭吸附效果产生重要影响，泥炭对复合重命属组分产生竞争性吸附。无论是批处理还是柱吸附方式，泥炭对重命属废水有很好的吸附效果，前者的出水质量和处理废水体积要高于后者，特别是针对低浓度重金属废水。泥炭对高浓度冶炼厂制酸废水的最佳处理工艺是化学沉淀预处理十泥炭吸附。尽管形态上发生了一定的变化，但碱处理后泥炭对受试重众属的吸附效果与天然泥炭相当，经过适当碱处理后可以获得腐技酸以增加泥炭的工业附加值。

厌氧产氢菌的分离筛选、诱变选育及其产氢特性的研究

本文从四川绵竹酒厂、成都市龙泉长安垃圾填埋场以及四川大学荷花池底的厌氧污泥中先后分离得到63株厌氧产氢菌，其中H-8、H-61、HC-10等16株产氢细菌产氢能力较高，HC-10的产氢能力最高，最大产氢量和最大产氢速率分别达到2840 ml H2/L培养基和25.39 mmol H2/g drycell·h，对HC-10进行生理生化鉴定和分子生物学鉴定，判定其为clostridium sp.，对HC-10的产氢条件进行了研究，结果表明，该菌的最适生长温度为35 ℃，最适生长初始pH为7，以葡萄糖为最佳碳源，以蛋白胨为最佳氮源，不利用无机氮源，其产氢发酵液相产物以乙醇和乙酸为主，其发酵类型属于乙醇型发酵。此外，以酒糟废液作为底物，进行了菌株HC-10的生物强化试验，研究表明，投加了HC-10的强化系统其产氢量比对照高出40.32%。 同时为了获得厌氧产氢菌的高效突变株，分别以产氢菌H-8和H-61为原始菌株进行微波诱变处理，对微波诱变参数进行了优化，考察了突变株的遗传稳定性、产氢特性及耐酸性。菌株H-8经过微波诱变得到5株高产氢突变株HW7、HW33、HW181、HW184、HW195，经多次传代表明HW195是稳定的高产突变株。突变株HW195具有较好的耐酸性，在pH值为2.8时仍能生长。通过间歇发酵实验，其最大产氢量和最大产氢速率分别达到2460 mL/L培养基和27.97 mmol H2/g drycell·h，比原始菌分别提高了50.75%和41.7%。菌株H-61经过微波诱变后选育得到的突变株HW-18，其最大产氢量和最大产氢速率分别达到2190 mL/L培养基和25.86 mmol H2/g drycell·h，比原始菌分别提高了23.03%和31.00%。 为了对比各种诱变方式对产氢菌产氢能力的影响，以厌氧产氢菌H-61为原始菌株，先后经亚硝基胍(NTG)、紫外(UV)诱变，选育得到1株高产突变株HCM-23。在葡萄糖浓度为10 g/L的条件下，其产氢量为3024 mL/L培养基，比原始菌株提高了69.89%；其最大产氢速率为33.19 mmol H2/g drycell·h，比原始菌株提高了68.14%。经过多次传代实验，稳定性良好。其发酵末端产物以乙醇和乙酸为主，属于典型乙醇型发酵。其最适产氢初始pH为6.5，最适生长温度为36 ℃，以蔗糖为最佳碳源。与原始菌株相比，突变株HCM-23的产氢特性发生了改变，如生长延滞期延长，可利用无机氮源等。 From anaerobic activated sludge, 16 strains of hydrogen producing bacteria were newly isolated. One of them named as HC-10 had the highest hydrogen producing capability, under the batch fermentative hydrogen production condition, the maximal hydrogen yield and hydrogen production rate was 2840 mL/L culture and 25.39 mmol H2/g drycell·h. It was identified as clostridium sp.HC-10 by 16S rDNA sequence analysis. Various parameters for hydrogen production, including substrates, initial pH and temperature, have been studied. The optimum condition for hydrogen producing of strain HC-10 were achieved as: initial pH 7.0, temperature 35 ℃, glucose as the favorite substrate, Moreover, using distiller's solubles wastewater as substrate, HC-10 strain was added in the biohydrogen producing system to research the bioaugmentation effection. The results showed that the hydrogen production of bioaugmentation system was 40.32% higher than the noaugmentation system. An anaerobic, hydrogen producing strain H-8 was irradiated by microwave to optimize the microwave mutagenesis condition, and to test the heredity, hydrogen-producing potential and aciduric of the mutants. An aciduric mutant named as HW195 with steady hydrogen-producing capability was obtained, which can grow at pH 2.8. Its capability of hydrogen production was tested in the batch culture experiments. The maximum hydrogen yield and hydrogen production rate was 2460 mL/L culture and 29.97 mmol H2/g drycell·h, which was 50.7% and 41.7% higher than those of the initial strain, respectively. When used the strain H-61 as original strain, a mutant named as HW18 was obtained. The maximum hydrogen yield and hydrogen production rate was 2190 mL/L culture and 25.86 mmol H2/g drycell·h, which was 23.03% and 31.00% higher than those of the initial strain, respectively. The results demonstrated that microwave mutagenesis could be used in the field of hydrogen producing microorganism. The hydrogen producing strain H-61 was used as an original strain which was induced by NTG and UV for increasing and the hydrogen production capability. One of the highest efficient H2-producing mutants was named as HCM-23 with its stable hydrogen production capability. which was tested in the batch culture experiments. With the condition of 10 g/L glucose, its cumulative hydrogen yield and hydrogen production rate was 3024 mL/L culture and 33.19 mmol H2/g drycell·h, 69.89％and 68.14％ higher than that of the original strain, respectively. The terminal liquid product compositions showed that the mutant HCM-23 fermentation was ethanol type, while the original strain H-61 fermentation was butyric acid type. Varieties of parameters of hydrogen production fermentation were studied, including time, carbon source, nitrogen source, glucose concentration, glucose utilization, initial pH and incubation temperature had been studied, indicated the optimum condition of hydrogen production for the mutant HCM-23 as initial pH6.5, temperature 36 ℃, and the favorite substrate was sucrose. The hydrogen production characters of the mutant and the original strain were different, such as, the growth lag phase and the utilization of inorganic nitrogen source, etc. This work shows a good application potential of NTG-UV combined mutation in the biohydrogen production. And the hydrogen production mechanism and metabolic pathway should be explored furthermore.

亚硝化—厌氧氨氧化处理猪场废水研究

猪场废水COD浓度高、氨氮浓度高、悬浮物浓度高，已成为农村面源污染的主要来源，并严重威胁到农村饮用水安全。猪场废水氨氮浓度高、处理难度大，如何采用经济高效的方法，去除氨氮使其达到排放标准，一直是猪场废水处理中面临的重要难题。 厌氧氨氧化是近年受到国内外水处理研究者广泛关注的新型生物脱氮技术，具有不需要外加有机碳源、节省供氧量、降低能耗等优点。虽然国内外研究者对厌氧氨氧化过程的脱氮机理、厌氧氨氧化菌的生理生化特性等进行了多方面的研究，但已有的报道大多以模拟废水为研究对象，以猪场废水为研究对象的报道，在国内外文献中极少有报导。 本论文以猪场废水为主要研究对象，考察了猪场废水的亚硝化过程、厌氧氨氧化的启动过程，并对亚硝化和厌氧氨氧化联合用于猪场废水脱氮进行了探索。 1．论文首先研究了猪场废水的亚硝化过程，考察了废水水质和主要运行条件对亚硝化过程的影响。实验表明：（1）亚硝化阶段反应时间为8到10h时，出水中氨氮和亚硝酸盐浓度比可达到1：1～1：1.23，满足厌氧氨氧化反应对二者比例的要求；达到前述要求时，氨氮去除率达到58.3～65.6 %，亚硝化率在整个过程均保持在97 %以上，COD去除率在59.2～68.6 %；（2）曝气量（溶解氧）对亚硝化过程影响显著，随着曝气量增大，达到厌氧氨氧化要求的氨氮与亚硝酸盐氮浓度比例所需水力停留时间τ越短，pH出现明显下降的时间越短；（3）τ对应的pH在7.8～8.1之间，无需进行pH调节即可满足厌氧氨氧化反应对pH的要求；（4）氨氮和COD降解过程遵循一级反应动力学，氨氮和COD降解的速率常数分别为0.0656～0.0724 1/h和0.0491～0.0664 1/h。 2．在进行亚硝化过程研究的同时，以模拟废水为试验对象，进行厌氧氨氧化启动研究。以反硝化污泥和养殖厂储水池厌氧底泥的混合污泥作为接种污泥，历时大约100天，培育出具有厌氧氨氧化活性的污泥，氨氮和亚硝酸盐氮最高进水浓度分别为223.8 mg/L和171.4 mg/L，去除率最高分别达48%和41.5%，此时二者消耗比例为1.33：1。 3．在猪场废水的亚硝化研究完成和厌氧氨氧化过程初步启动成功后，在模拟废水中逐步加入猪场废水的亚硝化处理出水，逐步实现亚硝化和厌氧氨氧化的组合。亚硝化出水添加到厌氧反应器后，厌氧氨氧化反应仍可继续进行，且去除效率逐步提高。研究发现添加的亚硝化出水中携带的亚硝化细菌在厌氧氨氧化菌膜外层生长并累积，增加了厌氧氨氧化反应基质的传质阻力，妨碍了厌氧氨氧化效率的提高。 4．亚硝化－厌氧氨氧化实际工程应用探索中，生物接触氧化池可在有效去除废水中的有机物的同时实现亚硝化，出水中氨氮和亚硝酸盐比例平均为1.10，可满足后续厌氧氨氧化的要求；在适宜的进水浓度和温度下，ABR池出现了厌氧氨氧化启动的迹象；研究同时发现，水质的波动和气温的变化是工程中影响厌氧氨氧化菌活性的重要因素。 论文的主要创新点在于：（1）以猪场废水为研究对象，以实现厌氧氨氧化为目标，对亚硝化过程进行了比较详细的考察，获得了亚硝化出水满足厌氧氨氧化要求的工艺条件，通过对其COD和氨氮降解过程的考察，得出亚硝化阶段COD降解和氨氮去除的动力学模型；（2）对亚硝化－厌氧氨氧化处理猪场废水进行了探索，确立了影响其污染物去除率稳定的重要因素。 论文的上述研究成果，为厌氧氨氧化技术的实用性研究提供理论依据。 Piggery wastewater, which is characterized by high concentration of COD、ammonium and suspend substance, has become a most important source of non-point source pollution and also severely threats drinking water security in rural area. How to discharge piggery wastewater with the ammonium concentration meeting standard by economical and effective method? This is the most urgent problem in piggery wastewater treatment. As a new biological nitrogen removal technology, Anammox process has been paid more and more attention by researchers all over the world. Anammox has advantages of no need of organic carbon addition, low oxygen consumption and energy consumption. Plenty of investigations have been carried out to the mechanism, physiological and biochemical characteristic of bacteria about Anammox. Most of researches focused on synthetic wastewater, there is rare report about its application in piggery wastewater. In this paper，experimental studies were performed to investigate Sharon process in treatment of piggery wastewater，the start up process of Annammox using synthetic wastewater were studied, the feasibility of applying Sharon-Anammox process in the nitrogen removal of piggery wastewater was evaluated. 1. Sharon process of piggery wastewater was firstly investigated to analyze the effects of water quality and main running parameters, which meet the NH4+-N to NO2--N ratio requirement of successive Anammox. Results showed: (1)During Sharon Process，after 8～10 hours’ reaction the NH4+-N to NO2--N ratio in effluent reached 1:1.0～1:1.23, when the removal percentage of NH4+-N was 58.3～65.6 %, a semi-nitration rate of above 97 % was achieved during the process; meanwhile 59.2～68.6 % of the COD was also removed. (2)The aeration rate（oxygen） had obvious effect on the hydraulic retention time(τ) which met the NH4+-N to NO2--N ratio requirement of Anammox. As aeration rate increased, the hydraulic retention time(τ) was shortened. (3) The pH corresponding to τ was between 7.8 and 8.1, thus it needed no artificial adjustment. (4) The reduction of ammonia and COD followed the first-order reaction kinetics. The velocity constants of ammonia and COD were 0.0656～0.0724 1/h and 0.0491～0.0664 1/h, respectively. 2. The startup of Anammox process using the artificial wastewater was performed simultaneously with Sharon. The aim was to investigate the running parameters of Anammox and make foundation for the combination stage. By using the mixture of denitrifying sludge and anaerobic sludge in tank of the breeding factory, sludge of Anammox activity was cultivated in UASB after 100 days. The removal percentage of NH4+-N and NO2-N were up to 48% and 41.5%, respectively, when the NH4+-N and NO2-N influent concentration were 223.8 mg/L and 171.4 mg/L, respectively, the NH4+-N and NO2-N removal rate was 1.33:1. 3. After investigation of Sharon and startup of Anammox, effluent of Sharon process was added into the synthetic wastewater to combine Sharon and Anammox step by step. It took some time after the addition of Sharon effluent that Anammox reaction continued and the removal rate kept increasing. It indicated that nitrifying bacteria were carried by the Sharon effluent cumulated in the outer layer of Anammox. This enhanced transfer resistance of Anammox reaction and the increasing removal rate was restrained. 4. In the bio-contact oxidation pond of practical project, Sharon process were carried out successfully and organic compounds were removed effectively. An average NO2-N/ NH4+-N rate of 1:1.0 was achieved in the effluent, which met the requirement of successive Anammox. Under condition of suitable influent concentration and temperature, there was evidence that Anammox could start up in ABR. The variety of wastewater and temperature had great affects on Anammox activity in practical engineering. Innovation of this paper: (1) The Sharon process for treating piggery wastewater was discussed in details. Technological parameters that met requirement of Anammox were obtained. The dynamic models of COD and ammonium removal in the process were educed. (2) Sharon-Ananmmox for treatment of piggery wastewater was investigated, and the primary influencing factors was studied. This paper could be a theoretical consult for research of Anammox utility.