保藏温度对厌氧氨氧化颗粒污泥特性的影响

为考察保藏温度对厌氧氨氧化污泥颗粒特性的影响,同时优化保藏厌氧氨氧化颗粒污泥温度参数,本试验首先通过HRT调控进水基质负荷培养厌氧氨氧化颗粒污泥,并采用KHCO3和Na HCO3交替提供无机碳源。然后分别在–40℃、4℃、(27±4)℃室温和35℃条件下避光保藏。结果表明,Na HCO3可代替KHCO3作为厌氧氨氧化菌生长的无机碳源。相比于其他保藏温度,4℃保藏能够较好地维持生物量和生物活性,同时能较好地维持颗粒污泥的沉降性能、颗粒污泥和细胞结构完整性。在保藏过程中,一阶衰减指数模型可拟合厌氧氨氧化颗粒污泥生物量及活性的衰减过程,衰减指数与胞溶程度正相关,而且生物量的衰减比活性的衰减更快。同时,颗粒污泥胞外聚合物中蛋白质与多糖的比值(PN/PS)和血红素不能有效指示保藏过程中颗粒污泥沉降性能和活性的变化,而生物活性与胞溶程度呈负相关。     

Denitrification characteristics of reject water in upflow biofiltration

Two types of bench-scale experiments using upflow biofilm reactors packed with granular floating polystyrene (GFP) or polyurethane foam cubes (PFC), were used to investigate the denitrification of reject water. A high denitrification rate was achieved in both upflow biofilm reactors since the highly concentrated volatile fatty acids in reject water served as effective hydrogen donors for denitrification. Of the two biofiltrations, the denitrification rate using GFP was 3.5 kg⁻¹ N m⁻³ per day, and higher than that using PFC. The amount of total attached biomass and solid capture capacity were also greater in GFP than in PFC. Moreover, the backwashing of the GFP packed column was optimized with air and water agitation. Of the processes investigated in this study, upflow biofiltration using GFP was the most acceptable process for reject water treatment based on treatability and operation.     

厌氧氨氧化菌脱氮机理及其在污水处理中的应用

厌氧氨氧化细菌(anammox)可以将亚硝酸盐和氨氮转化为氮气从而缩短氨氮转化的过程,它已经成为新型生物污水脱氮技术研究的热点之一。当前,有关厌氧氨氧化菌特有的生理结构特点、种群分类及其功能酶等方面的研究取得了一定突破,为实现其工业应用奠定了良好的理论基础;同时分子生物学技术在厌氧氨氧化细菌种群分布、群落多样性及其共生关系等方面的应用也大大促进了污水生物脱氮技术的革新和进步。总结了厌氧氨氧化菌主要的生理生化特点、细胞结构特点、脱氮机理、污水处理体系中的应用以及分子生物学方法对污水处理体系中厌氧氨氧化菌种群分析的研究现状,并指出未来anammox细菌在生物特性及在污水脱氮处理实际应用的研究中的热点问题。生物特性方面的主要研究热点有：（1）anammox细菌除厌氧氨氧化作用外,其它新陈代谢途径有待探索;（2）anammox细菌在不同环境中分布的倾向性问题;（3）新型anammox细菌的确定。污水处理的实际应用方面的主要研究热点有：（1）anammox污泥的快速高效富集问题;（2）设计高特异性引物;（3）anammox细菌和其他微生物的共生关系。     

Start-up and inhibition analysis of the Anammox process seeded with anaerobic granular sludge

The longer start-up period of the Anammox process is due to the very low cellular yield and growth rates of Anammox bacteria. Nitrite inhibition is considered to be the key factor in the instability of the Anammox process during the operation. However, little attention was paid to the inhibitory effect of pH and free ammonia. This paper presents start-up and inhibition analysis of an Anammox biofilm reactor seeded with anaerobic granular sludge. Results showed that the start-up period could be divided into the sludge lysis phase, lag phase, propagation phase, stationary phase and inhibition phase. Optimization control could be implemented correspondingly to accelerate the start-up of Anammox bioreactors. Effluent pH increased to 8.7–9.1 when the nitrogen removal rate was higher than 1,200 mg l⁻¹ day⁻¹. The free ammonia concentration was accompanied with a higher level of 64–73 mg l⁻¹. Inhibitory effects of high pH and free ammonia on Anammox bacteria contributed to the destabilization of the Anammox bioreactor during the first 125 days with influent KHCO₃ of 0.5 g l⁻¹. Increasing the suffering capacity in the inlet by dosing 1.25 g KHCO₃ l⁻¹ effectively reduced the pH variation, and the nitrogen removal performance of the reactor was further developed.     

厌氧氨氧化启动过程Anammox菌富集规律和差异分析

为明确厌氧氨氧化反应器启动过程中Anammox菌的富集规律,采用荧光原位杂交(FISH)和实时荧光定量PCR(q-PCR)分析技术,对未添加填料、添加多面空心球以及添加竹炭的3个UASB反应器厌氧氨氧化启动过程中Anammox菌的增长规律进行分析。研究表明,Anammox菌的相对数量和绝对数量均随着启动时间呈逐渐递增趋势,在稳定运行阶段的第123天,无填料、多面空心球和竹炭反应器中Anammox菌分别占总细菌的23.3%、32.6%和43.7%,单位VSS污泥中Anammox菌16S rRNA基因拷贝数分别为(25.64±2.76)×107、(47.12±2.76)×107和(577.99±27.25)×107拷贝数g–1 VSS。竹炭反应器中Anammox菌最大生长率和最短倍增时间分别为0.064 d?1和10.8 d,最大生长率分别是无填料和多面空心球反应器的1.78倍和1.88倍。因此,填料添加特别是竹炭的添加可极大地促进Anammox菌的选择性生长和繁殖。FISH和q-PCR分析技术均适用于Anammox菌的富集规律研究,但因其检测目标存在差异,造成两者表征结果有所不同。     

Anammox反应器启动过程中颗粒污泥性状变化特性

以厌氧颗粒污泥作为接种物,通过185 d的运行,成功启动了上流式厌氧氨氧化污泥床(Upflow anaerobic sludge blanket,UASB)反应器。反应器的进水氨氮与亚硝氮浓度分别提升至224 mg/L和255 mg/L,容积氮去除速率提升至3.76 kg/(m3·d)。采用红外光谱、扫描电镜和透射电镜等对厌氧氨氧化颗粒污泥的性状进行观察,发现颗粒污泥在启动过程中经历了污泥颗粒裂解到污泥颗粒重组的过程,且厌氧氨氧化颗粒污泥表面含有丰富的官能团,说明厌氧氨氧化颗粒污泥可能具有良好的吸附性能。采用宏基因组测序的方法对启动前后颗粒污泥的生态结构进行分析,发现原接种污泥优势菌群(变形菌门、厚壁菌门、拟杆菌门)丰度大幅减少,厌氧氨氧化菌所属的浮霉状菌门丰度则由1.59%提升到23.24%。     

厌氧反应器中颗粒污泥的培育及应用研究进展*

厌氧生物处理技术因其具有有机负荷高、污泥产量低、能耗低等优点被广泛应用于各种废水处理中。厌氧颗粒污泥具有沉降性能好、微生物浓度高、有机负荷高等优点,极大地提高了废水处理效率。尤其在处理含高氨氮废水中,厌氧颗粒污泥的形成对反应器的高效生物脱氮至关重要。但到目前为止,厌氧反应器中的颗粒污泥形成及废水处理效果还缺乏系统的认识。鉴于此,总结了厌氧反应器中颗粒污泥的形成机制,分析了影响厌氧反应器中颗粒污泥形成的因素,论述了厌氧反应器中厌氧颗粒污泥生长的模拟,最后介绍了厌氧颗粒污泥在国内外的主流应用。厌氧反应器中颗粒污泥的形成是综合因素影响的结果,对影响厌氧颗粒污泥形成的每个因素都需要认真对待,可为在厌氧反应器中颗粒污泥的培育和应用提供理论指导和技术支撑。     

厌氧铵氧化过程中关键酶及相关分子标记在生态学研究中的应用进展

厌氧铵氧化是由微生物介导的氮素循环过程中的重要途径之一。近20年来,通过对厌氧铵氧化细菌生态学、基因组学和生理代谢特性的探索,人们对其微生物学机制已经有了较多的认识:厌氧铵氧化细菌通过亚硝酸盐还原酶将亚硝酸根离子还原为一氧化氮,进而与铵离子结合在联氨合成酶的作用下生成联氨,最后通过联氨氧化酶的催化产生终产物氮气。同时,对参与这些过程的关键酶及其功能基因的认识有助于选择新的分子标记,从而为研究厌氧铵氧化细菌的多样性和分子生态学特征提供新的工具,以弥补16S rRNA基因特异性相对较低且难以与生态功能关联等方面的不足。对目前已知的参与厌氧铵氧化过程的3种关键酶的研究历程和现状进行了评述,并总结了利用3种功能基因进行厌氧铵氧化细菌生态学研究的最新进展。     

Importance of the operating pH in maintaining the stability of anoxic ammonium oxidation (anammox) activity in moving bed biofilm reactors

Two bench-scale parallel moving bed biofilm reactors (MBBR) were operated to assess pH-associated anammox activity changes during long term treatment of anaerobically digested sludge centrate pre-treated in a suspended growth partial nitrification reactor. The pH was maintained at 6.5 in reactor R1, while it was allowed to vary naturally between 7.5 and 8.1 in reactor R2. At high nitrogen loads reactor R2 had a 61% lower volumetric specific nitrogen removal rate than reactor R1. The low pH and the associated low free ammonia (FA) concentrations were found to be critical to stable anammox activity in the MBBR. Nitrite enhanced the nitrogen removal rate in the conditions of low pH, all the way up to the investigated level of 50 mg NO₂-N/L. At low FA levels nitrite concentrations up to 250 mg NO₂-N/L did not cause inactivation of anammox consortia over a 2-days exposure time.     

Measurement of heat transfer coefficients in stirred single‐use bioreactors by the decay of hydrogen peroxide

Single‐use bioreactors are barely described by means of their heat transfer characteristics, although some of their properties might affect this process. Steady‐state methods that use external heat sources enable precise investigations. One option, commonly present in stirred, stainless steel tanks, is to use adjustable electrical heaters. An alternative are exothermic chemical reactions that offer a higher flexibility and scalability. Here, the catalytic decay of hydrogen peroxide was considered a possible reaction, because of the high reaction enthalpy of –98.2 kJ/mole and its uncritical reaction products. To establish the reaction, a proper catalyst needed to be determined upfront. Three candidates were screened: catalase, iron(III)‐nitrate and manganese(IV)‐oxide. Whilst catalase showed strong inactivation kinetic and general instability and iron(III)‐nitrate solution has a pH of 2, it was decided to use manganese(IV)‐oxide for the bioreactor studies. First, a comparison between electrical and chemical power input in a benchtop glass bioreactor of 3.5 L showed good agreement. Afterwards the method was transferred to a 50 L stirred single‐use bioreactor. The deviation in the final results was acceptable. The heat transfer coefficient for the electrical method was 242 W/m²/K, while the value achieved with the chemical differed by less than 5%. Finally, experiments were carried out in a 200 L single‐use bioreactor proving the applicability of the chemical power input at technical relevant scales.     

Aerobic granular sludge: characterization,mechanism of granulation and application to wastewater treatment

Aerobic granular sludge can be classified as a type of self-immobilized microbial consortium, consisting mainly of aerobic and facultative bacteria and is distinct from anaerobic granular methanogenic sludge. Aerobic granular technology has been proposed as a promising technology for wastewater treatment, but is not yet established as a large-scale application. Aerobic granules have been cultured mainly in sequenced batch reactors (SBR) under hydraulic selection pressure. The factors influencing aerobic granulation, granulation mechanisms, microbial communities and the potential applications for the treatment of various wastewaters have been studied comprehensively on the laboratory-scale. Aerobic granular sludge has shown a potential for nitrogen removal, but is less competitive for the high strength organic wastewater treatments. This technology has been developed from the laboratory-scale to pilot scale applications, but with limited and unpublished full-scale applications for municipal wastewater treatment. The future needs and limitations for aerobic granular technology are discussed.     

Targeted metagenomics reveals extensive diversity of the denitrifying community in partial nitritation anammox and activated sludge systems

The substantial presence of denitrifiers has already been reported in partial nitritation anammox (PNA) systems using the 16S ribosomal RNA (rRNA) gene, but little is known about the phylogenetic diversity based on denitrification pathway functional genes. Therefore, we performed a metagenomic analysis to determine the distribution of denitrification genes and the associated phylogeny in PNA systems and whether a niche separation between PNA and conventional activated sludge (AS) systems exists. The results revealed a distinct abundance pattern of denitrification pathway genes and their association to the microbial species between PNA and AS systems. In contrast, the taxonomic analysis, based on the 16S rRNA gene, did not detect notable variability in denitrifying community composition across samples. In general, narG and nosZa2 genes were dominant in all samples. While the potential for different stages of denitrification was redundant, variation in species composition and lack of the complete denitrification gene pool in each species appears to confer niche separation between PNA and AS systems. This study suggests that targeted metagenomics can help to determine the denitrifying microbial composition at a fine‐scale resolution while overcoming current biases in quantitative polymerase chain reaction approaches due to a lack of appropriate primers.     

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。     

Development of a novel process for the biological conversion of H2S and methanethiol to elemental sulfur

The feasibility of anaerobic treatment of wastewater containing methanethiol (MT), an extremely volatile and malodorous sulfur compound, was investigated in lab-scale bioreactors. Inoculum biomass originating from full-scale anaerobic wastewater treatment facilities was used. Several sludges, tested for their ability to degrade MT, revealed the presence of organisms capable of metabolizing MT as their sole source of energy. Furthermore, batch tests were executed to gain a better understanding of the inhibition potential of MT. It was found that increasing MT concentrations affected acetotrophic organisms more dramatically than methylotrophic organisms. Continuous reactor experiments, using two lab-scale upflow anaerobic sludge bed (UASB) reactors (R1 and R2), aimed to determine the maximal MT load and the effect of elevated sulfide concentrations on MT conversion. Both reactors were operated at a hydraulic retention time (HRT) of about 7 hours, a temperature of 30 degrees C, and a pH of between 7.3 and 7.6. At the highest influent MT concentration applied, 14 mM in R1, corresponding to a volumetric loading rate of about 50 mM MT per day, 87% of the organic sulfur was recovered as hydrogen sulfide (12.2 mM) and the remainder as volatile organic sulfur compounds (VOSCs). Upon decreasing the HRT to 3.5 to 4.0 h at a constant MT loading rate, the sulfide concentration in the reactor decreased to 8 mM and MT conversion efficiency increased to values near 100%. MT conversion was apparently inhibited by the high sulfide concentrations in the reactor. The specific MT degradation rate, as determined after 120 days of operation in R1, was 2.83 +/- 0.27 mmol MT g VSS(-1) day(-1). During biological desulfurization of liquid hydrocarbon phases, such as with liquefied petroleum gas (LPG), the combined removal of hydrogen sulfide and MT is desired. In R2, the simultaneous addition of sodium sulfide and MT was therefore studied and the effect of elevated sulfide concentrations was investigated. The addition of sodium sulfide resulted in enhanced disintegration of sludge granules, causing significant washout of biomass. Additional acetate, added to stimulate growth of methanogenic bacteria to promote granulation, was hardly converted at the termination of the experimental period.     

Biodegradability and toxicity of styrene in the anaerobic digestion process

Start-up and operation of an Upflow Anaerobic Sludge Blanket (UASB) reactor fed with an industrial effluent from a polymer synthesis plant containing 6 mg styrene l^–1 was unstable. In batch assays with 200 mg styrene l^–1, 74% of styrene was degraded at a rate of 7 ml methane g^–1 volatile suspended solids.day, without a lag phase. The toxicity limit (IC₅₀) of styrene was 1.4 mM for the acetoclastic activity, 0.45 and 1.6 mM for the methanogenic activity in the presence of 30 mM of propionate and ethanol respectively. Instability of UASB operation was attributed to other compounds such as acrylates or detergents present in the industrial effluent.     

High-yield production of oxalic acid for metal leaching processes by Aspergillus niger

Abstract The complex-forming compound oxalic acid can effectively solubilise metals such as aluminium, iron, lithium, and manganese. In order to produce high amounts of oxalic acid for biohydrometallurgical processes, it was the aim of this work to optimise oxalic acid production by Aspergillus niger , a fungus well known for its ability to produce oxalic acid. A. niger excreted 427 mmol oxalic acid 1⁻¹ if it was cultivated in a pH-controlled (pH 6.0) fed-batch run in a 2-1 stirred tank reactor. Sucrose and lactose permeate were suitable carbon sources for oxalic acid production. In sucrose medium, A. niger produced high amounts of gluconic and oxalic acids, whereas in lactose permeate medium only oxalic acid was produced. Cultivation in green syrup and molasses media lead to high yields of biomass, but low oxalic acid production (<20 mmol 1⁻¹).