单室微生物电解池除镍途径分析及微生物群落动态特征北大核心CSCD

【目的】为探究UASB颗粒污泥启动的单室微生物电解池(Single-chamber microbial electrolysis cell,SMEC)对Ni(II)的去除途径和SMEC中微生物群落的动态特征。【方法】以乙酸钠为底物,采用单因子控制方法分析SMEC对Ni(II)的去除途径和应用Illumina高通量测序技术解析SMEC启动过程中微生物群落的组成和结构动态学特征。【结果】结果表明,SMEC对重金属的去除主要通过吸附和微生物作用。经培养驯化功能菌群发生变化。成熟单室微生物燃料电池(Single-chamber microbial fuel cell,SMFC)阳极生物膜菌群主要是Proteobacteria(变形菌门,91.42%)中的Geobacter sp.(地杆菌属,76.25%);阴极生物膜菌群主要是Bacteroidetes(拟杆菌门,47.99%)中的Niabella sp.(布鲁氏菌属,33.01%)和Proteobacteria(45.74%)中的Ochrobactrum sp.(苍白杆菌属,10.80%)。成熟SMFC改装成的SMEC在12.5 mg-Ni(II)/L下,阳极生物膜菌群由单一优势菌Geobacter sp.转变为Geobacter sp.(41.56%)和Proteobacteria中的Azospirillum sp.(固氮螺菌属,5.97%);阴极生物膜菌群由Niabella sp.和Ochrobactrum sp.转变为Firmicutes(厚壁菌门,25.21%)中的Acetoanaerobium sp.(19.28%)、Proteobacteria(51.42%)中的Dokdonella sp.(16.48%)和Azospirillum sp.(9.49%)。【结论】本研究表明,污泥微生物经SMFC和SMEC驯化过程及Ni(II)的淘汰和选择,在电极上形成了稳定、高效产电与除镍菌群,优势菌群为Proteobacteria。     

利用微生物电解池处理牛奶废水过程中产电菌落与产氢性能之间的关系

【目的】 研究微生物电解池(Microbial electrolysis cell, MEC)利用复杂有机物作为底物的运行特性, 对其在废水处理中的应用有着重要的意义。【方法】 以模拟牛奶废水为基质, 通过构建MEC反应器来考察在不同外加电压条件下产电菌群的性能。【结果】 当外加电压升高到1.2 V时, 最大电流密度可达到261 A/m3, 产氢速率可达0.048 m3 H2/m3 d, 分别比外加电压为0.4 V的情形提高了467%和700%。外加电压为1.2 V时, 系统对COD和蛋白质去除率可分别达59%和74%, 其中COD去除较之0.4 V的情形提高了22.5%。PCR-DGGE的分子生物学分析结果表明, 阳极生物膜中以Geobacter sp.作为优势菌, 说明在利用大分子有机物作为基质时产电菌与非产电菌的协同作用更为明显。【结论】 MEC能够利用牛奶废水作为燃料, 在实现高效降解的同时以产氢的形式进行能量产出, 这为MEC的实际应用提供了研究思路。     

好氧-厌氧混合污泥启动微生物燃料电池产电性能及微生物群落动态特征

【目的】为探讨好氧-厌氧混合污泥启动微生物燃料电池(Microbial fuel cell,MFC)产电性能以及MFC对微生物群落的选择作用,【方法】以乳酸为底物,应用不依赖于培养的微生物分子生物学技术解析单室MFC启动过程中微生物群落的组成和结构动态学特征。【结果】结果表明,MFC经过3个周期启动成功,最高输出电压230 m V。当MFC外电阻为1656Ω时,最大功率密度11.15 W/m3,电池运行稳定。混合污泥启动MFC以后,阳极生物膜微生物群落结构同种泥差异较大,且多样性降低。生物膜中微生物类群按丰度依次为β-变形菌纲(Betaproteobacteria)24.90%、拟杆菌门(Bacteroidetes)21.30%、厚壁菌门(Firmicutes)9.70%、γ-变形菌纲(Gammaproteobacteria)8.50%、δ-变形菌纲(Deltaproteobacteria)7.90%、绿弯菌门(Chloroflexi)4.20%以及α-变形菌纲(Alphaproteobacteria)3.60%。有利于生物膜形成与稳定的动胶菌属(Zoogloea)和不动杆菌属(Acinetobacter)序列丰度分别占生物膜群落的5.00%和3.90%,与MFC产电能力直接相关的地杆菌属(Geobacter)序列由混合污泥中的0.60%上升至阳极生物膜中的2.60%。【结论】本研究表明,MFC阳极生物膜在驯化过程中对污泥中的微生物进行淘汰和选择,最终驯化形成了有利于生物膜形成与稳定、有机物厌氧发酵与产电的微生物菌群。     

驯化对生物阴极微生物燃料电池中阴极微生物群落多样性的影响

【背景】生物阴极微生物燃料电池因其构造成本低和阴极可持续性发展的优点而成为一种很有前途的废水处理系统,但阴极微生物的氧化还原性能限制了其在实际应用中的推广。【目的】为了提高生物阴极的性能,需要深入了解影响阴极氧化还原性能的微生物群落。【方法】利用16S rRNA基因高通量测序技术分析对比原始接种污泥样品和驯化后阴极电极上生物膜样品多样性及结构变化。【结果】测序结果表明,原始接种污泥样品与驯化后阴极电极生物膜样品中微生物群落种类和结构存在显著差异,驯化后阴极电极生物膜样品中变形菌门(Proteobacteria)、γ-变形菌纲(Gammaproteobacteria)和特吕珀菌属(Trueperaceae)相对丰度比例高于原始污泥样品,成为优势菌群。【结论】驯化对系统阴极电极生物膜群落影响显著,随着产电量的输出,优势菌群不断富集,最终形成一个适应该实验环境下的新的微生物群落。对优势菌群结构和变化进行探讨,为生物阴极的研究补充更多生物学方面的理论基础。     

Mcc在脱色希瓦氏菌S12电极呼吸中的作用

【目的】研究脱色希瓦氏菌S12周质空间c型细胞色素Mcc的功能,进一步探索和补充微生物胞外电子传递过程的机制。【方法】借助自杀质粒敲除mcc基因,通过细胞浓度测定和激光共聚焦显微镜比较分析突变株和野生株之间的浮游细胞和生物膜的生长情况,并比较分析二者在微生物燃料电池电极还原、铁还原和胞外偶氮染料还原过程中的功能。【结果】Mcc缺失对铁还原和偶氮还原没有影响,但却造成电极呼吸活性下降34.1%;与野生株相比,mcc突变株的好氧生长和厌氧浮游细胞生长无明显影响,但却显著抑制了电极表面生物膜的形成。【结论】Mcc是希瓦氏菌S12电极呼吸过程中周质空间电子传递的重要组分之一,缺失会显著抑制其电极呼吸效率以及生物膜的形成。     

一株耐盐产电菌Shewanella algae E-1的分离及其产电特性分析

【背景】产电微生物的种类和电化学活性机制对微生物燃料电池的产电性能有着重要的影响。【目的】从海水中分离获得一株耐盐产电微生物,研究其产电特性并鉴定种属信息。【方法】以取自南海的海水为接种液启动并运行阳极液中含有不同盐浓度的微生物燃料电池,从富集的阳极生物膜上分离得到一株纯培养的微生物菌株,命名为E-1。通过接种于阳极液中添加不同盐浓度的微生物燃料电池中对其产电特性进行分析,并利用形态学观察、Biolog分析和16SrRNA基因序列比对相结合的方法进行种属鉴定。【结果】菌株E-1在无外源添加和外源添加6.6%NaCl条件下产生的功率密度分别为51.69 m W/m2和26.56 m W/m2,这与其良好的耐盐能力相关。菌株E-1被鉴定为海藻希瓦氏菌(Shewanella algae),表现出多样的底物利用能力,生长的温度范围为25-40°C,pH范围为5.0-10.0。【结论】这是首次对Shewanella algae种内微生物产电性能及其在微生物燃料电池中应用的报道,丰富了产电微生物的多样性,菌株E-1能够在较高盐浓度条件下表现出良好的产电性能,为微生物燃料电池在海水资源化处理方面的应用提供新的实验材料。     

微生物燃料电池利用乳酸产电性能与微生物群落分布特征

【目的】为探讨以乳酸为基质的微生物燃料电池(Microbial fuel cell,MFC)产电性能以及微生物群落在阳极膜、悬浮液、阳极沉淀污泥中的分布特征,【方法】试验建立了双室MFC,以乳酸为阳极主要碳源,研究了反应器的启动过程及产电效能,同时以电镜和PCR-变性梯度凝胶电泳(Denaturing gradient gelelectrophoresis,DGGE)技术解析了微生物群落的空间分布特征。【结果】结果表明,反应器启动第7天时外电压达到0.56 V,当外阻为80Ω时,电流密度为415 mA/m2,MFC的功率密度达到最大值82 mW/m2。电镜观察发现大量杆菌附着在阳极表面,结合较为紧密;DGGE图谱显示阳极膜表面微生物与种泥最为相似,与阳极悬浮液、底部沉淀污泥中的主要菌群一致,条带序列与睾丸酮丛毛单胞菌(Comamonas testosteroni)和布氏弓形菌(Arcobacter butzleri)等最为相似。【结论】本研究表明以乳酸为基质MFC可产生较高的功率密度,阳极附着的优势菌与接种污泥来源密切相关。     

微生物燃料电池阳极微生物群落对乳酸-丙酸-乳酸底物转换的响应特征

摘要:【目的】为探讨底物波动对微生物燃料电池(MFC)产电效能和阳极微生物群落的影响,【方法】依次以乳酸-丙酸-乳酸为底物,应用不依赖于培养的微生物分子生态学技术,解析单室MFC 启动及底物替换过程中阳极微生物群落的动态学响应特征。【结果】底物的更换过程降低了MFC的产电效能,当改变为新底物后,MFC需要较长的产电恢复期。同时,底物的转换改变了阳极微生物群落结构,Anaeromusa spp.、Pseudomonas spp．以及Thiobacillus thioparus对乳酸底物具有很好的响应,随着乳酸底物的投加而富集;丙酸底物对Dechloromonas spp.和Comamonas testosteroni等类群表现出较强的选择作用;而产电微生物Geobacter spp.由于利用乳酸、丙酸的共同代谢产物乙酸为底物而被逐渐富集,是多种底物替换过程的重叠种群。【结论】本研究表明,MFC的阳极微生物群落组成与投加的底物有较强的对应性,为了减缓底物波动对MFC产电过程的影响,应尽量采用混合有机底物,以提供宽泛的营养生态位,提高种群的功能重叠性。     

寺河矿煤地质产甲烷微生物菌群的保藏和产甲烷性能

【背景】煤地质产甲烷微生物菌群可以代谢煤基质产生甲烷,对于实现煤层气资源的再利用具有重要意义。【目的】检测产甲烷菌群在保藏过程中群落结构的动态变化以及在产气实验中甲烷气的生成情况,以验证保藏方法的可行性,同时为煤层气的微生物增产奠定基础。【方法】分别于不同温度条件下比较3种菌种保藏方法,即甘油/L-半胱氨酸法、富营养法和煤基-基础盐法。通过产气实验检测不同保藏条件下产甲烷菌群的活力。同时,采用454高通量测序技术测定16S r RNA基因序列,分析25°C条件下煤基-基础盐菌种保藏过程中微生物群落结构的变化。【结果】比较了9组菌种保藏方法,发现菌种最佳保藏条件为25°C的煤基-基础盐保藏。在该条件下保藏的产甲烷菌群活性最高,甲烷生成量最大。以无烟煤为碳源进行产气实验时甲烷生成量为12%-25%,而以褐煤为碳源时甲烷生成量可达24%-73%。在25°C的煤基-基础盐菌种保藏条件下,保藏初期细菌的主要优势菌为假单胞菌属(Pseudomonas),而古菌的主要优势菌为甲烷八叠球菌属(Methanosarcina)。随着保藏时间的增加,细菌的群落结构变化显著,发酵细菌及产氢产乙酸细菌成为优势细菌,古菌的群落结构则相对稳定。【结论】菌种保藏的最佳条件为25°C的煤基-基础盐,保藏的产甲烷菌群能长期维持在较高的活性状态,具有较好的产甲烷能力。     

微生物燃料电池阳极产电微生物和阴极受体特性及研究进展

介绍微生物燃料电池的基本工作原理。根据电子传递方式阳极产电微生物分为无需中间体微生物和需中间体微生物。对阴极进行不同反应所涉及的最终电子受体进行了概述,并展望了微生物燃料电池的应用前景。     

Characterization of microbial communities during anode biofilm reformation in a two-chambered microbial electrolysis cell (MEC)

GeoChip (II) and single strand conformation polymorphism (SSCP) were used to characterize anode microbial communities of a microbial electrolysis cell (MEC). Biofilm communities, enriched in a two-chamber MEC (R1, 0.6 V applied) having a coulombic efficiency (CE) of 35±4% and a hydrogen yield (Y(H?))of 31±3%, were used as the inoculum for a new reactor (R2). After three months R2 achieved stable performance with CE=38±4% and (Y(H?)). Few changes in the predominant populations were observed from R1 to R2. Unlike sludge inoculation process in R1 in the beginning, little further elimination was aroused by community competitions in anode biofilm reformation in R2. Functional genes detection of biofilm indicated that cytochrome genes enriched soon in new reactor R2, and four genera (Desulfovibrio, Rhodopseudomonas, Shewanella and Geobacter) were likely to contribute to exoelectrogenic activity. This work also implied that symbiosis of microbial communities (exoelectrogens and others) contribute to system performance and stability.     

High hydrogen production rate of microbial electrolysis cell (MEC) with reduced electrode spacing

Practical applications of microbial electrolysis cells (MECs) require high hydrogen production rates and a compact reactor. These goals can be achieved by reducing electrode spacing but high surface area anodes are needed. The brush anode MEC with electrode spacing of 2 cm had a higher hydrogen production rate and energy efficiency than an MEC with a flat cathode and a 1-cm electrode spacing. The maximum hydrogen production rate with a 2 cm electrode spacing was 17.8 m(3)/m(3)d at an applied voltage of E(ap)=1 V. Reducing electrode spacing increased hydrogen production rates at the lower applied voltages, but not at the higher (>0.6 V) applied voltages. These results demonstrate that reducing electrode spacing can increase hydrogen production rate, but that the closest electrode spacing do not necessarily produce the highest possible hydrogen production rates.     

Enhancement of hydrogen production in a single chamber microbial electrolysis cell through anode arrangement optimization

Reducing the inner resistances is crucial for the enhancement of hydrogen generation in microbial electrolysis cells (MECs). This study demonstrates that the optimization of the anode arrangement is an effective strategy to reduce the system resistances. By changing the normal MEC configuration into a stacking mode, namely separately placing the contacted anodes from one side to both sides of cathode in parallel, the solution, biofilm and polarization resistances of MECs were greatly reduced, which was also confirmed with electrochemical impedance spectroscopy analysis. After the anode arrangement optimization, the current and hydrogen production rate (HPR) of MEC could be enhanced by 72% and 118%, reaching 621.3 ± 20.6 A/m³ and 5.56 m³/m³ d respectively, under 0.8 V applied voltage. A maximum current density of 1355 A/m³ with a HPR of 10.88 m³/m³ d can be achieved with 1.5 V applied voltage.     

Anode microbial communities produced by changing from microbial fuel cell to microbial electrolysis cell operation using two different wastewaters

Conditions in microbial fuel cells (MFCs) differ from those in microbial electrolysis cells (MECs) due to the intrusion of oxygen through the cathode and the release of H₂ gas into solution. Based on 16S rRNA gene clone libraries, anode communities in reactors fed acetic acid decreased in species richness and diversity, and increased in numbers of Geobacter sulfurreducens, when reactors were shifted from MFCs to MECs. With a complex source of organic matter (potato wastewater), the proportion of Geobacteraceae remained constant when MFCs were converted into MECs, but the percentage of clones belonging to G. sulfurreducens decreased and the percentage of G. metallireducens clones increased. A dairy manure wastewater-fed MFC produced little power, and had more diverse microbial communities, but did not generate current in an MEC. These results show changes in Geobacter species in response to the MEC environment and that higher species diversity is not correlated with current.     

基于多Agent仿真解析处理剩余污泥的微生物电解池种群互作关系

【背景】微生物电化学系统耦合了电化学反应和厌氧消化过程,在处理剩余污泥同时实现能源回收,成为具有应用前景的技术之一。揭示电活性生物膜和活性污泥种群互作机制,有助于进一步调控和强化系统性能。高通量核酸测序技术研究微生物群落具有投入大、耗时长和不可预测的缺点,开展微生物群落动态仿真可以更有效地预测群落结构与功能。【目的】研究厌氧消化和生物电化学系统的微生物种间热力学与动力学的演化规律。在考虑电子供体、电子受体、温度、pH值等生态条件下,分析底物的电子流向及微生物群落结构的动态变化。【方法】通过对剩余污泥处理的微生物电解池(Microbial electrolytic cell,MEC)建立一个多Agent仿真(Multi-agent-based simulation,MAS)模型,评估MEC对底物氧化电子转移的能量效率和传质效率,模拟微生物群落结构实时变化,同时耦合动力学和热力学分析;揭示影响MES运行的电子流向决定性因素及相应的微生物种群,为复杂污染物生物处理系统中种间互作和动力学研究提供基础依据。【结果】通过MAS模拟,确定MEC污泥处理工艺的最佳能量传递效率与传质效率为η=0.2,ε=0.5,MAS结合热力学与动力学参数模拟微生物的群落动态与实验组有较高的吻合性。在长期的运行中,微生物电化学系统中丙酮酸没有积累。【结论】证实了MAS结合热力学与动力学参数可以预测微生物的群落动态,并进行实时监测。研究表明多Agent仿真为微生物群落结构动态变化提供了一种新的研究方法,该方法与高通量核酸测序技术进行校验和联用,为人工和自然生态系统中微生物种群预测与评估研究提供一个新的手段。     

生物膜法强化净化氨氮污染水体及其微生物群落解析

【目的】比较不同营养条件及挂膜方式下生物膜法对氨氮污染水体的净化效果及其功能微生物群落结构。【方法】设置空白(Blank)、自然成膜(Raw)、预附脱氮菌强化挂膜(PCC)3组生物膜反应器,利用末端限制性片段长度多态性(T-RFLP)技术和非度量多维标度(NMDS)分析方法对生物膜反应器转化氨氮过程中微生物群落结构及其演替过程进行动态解析。【结果】在C/N=1:1时,除PCC在起始阶段短暂具有较高的氨氮脱除效率外,Blank、Raw和PCC最终均表现出较低的氨氮转化效率(10%-20%)。改变C/N=2:1后,Raw和PCC对人工合成污水中NH4+-N的转化率均提高至95%以上,而且Raw与PCC的群落结构在C/N=2:1时具有较高的相似性,优势菌群主要为γ-变形菌纲(Gammaproteobacteria)、放线菌纲(Actinobacteria)和硝化螺菌纲(Nitrospira)。【结论】C/N是影响生物膜反应器氨氮去除效果及驱动生物膜反应器中细菌群落结构发生改变的重要因子。     

A comparison of air and hydrogen peroxide oxygenated microbial fuel cell reactors

In this study, a two-compartment continuous flow microbial fuel cell (MFC) reactor was used to compare the efficiencies of cathode oxygenation by air and by hydrogen peroxide. The MFC reactor had neither a proton-selective membrane nor an electron transfer mediator. At startup, the cathodic compartment was continuously aerated and the anodic compartment was fed with a glucose solution. An increase of electrical power generation from 0.008 to 7.2 mW m(-2) of anode surface with a steady-state potential of 215-225 mV was observed within a period of 12 days. The performance of the air-oxygenated MFC reactor progressively declined over time because of biofilm proliferation in the cathodic compartment. Oxygenation of the cathodic compartment using 300 mL d(-1) of 0.3% hydrogen peroxide solution resulted in a power density of up to 22 mW m(-2) (68.2 mA m(-2)) of anode surface at a potential of 340-350 mV. The use of H2O2 for oxygenation was found to improve the long-term stability of the MFC reactor.     

Continuous power generation and microbial community structure of the anode biofilms in a three-stage microbial fuel cell system

A mediator-less three-stage two-chamber microbial fuel cell (MFC) system was developed and operated continuously for more than 1.5 years to evaluate continuous power generation while treating artificial wastewater containing glucose (10 mM) concurrently. A stable power density of 28 W/m³ was attained with an anode hydraulic retention time of 4.5 h and phosphate buffer as the cathode electrolyte. An overall dissolved organic carbon removal ratio was about 85%, and coulombic efficiency was about 46% in this MFC system. We also analyzed the microbial community structure of anode biofilms in each MFC. Since the environment in each MFC was different due to passing on the products to the next MFC in series, the microbial community structure was different accordingly. The anode biofilm in the first MFC consisted mainly of bacteria belonging to the Gammaproteobacteria, identified as Aeromonas sp., while the Firmicutes dominated the anode biofilms in the second and third MFCs that were mainly fed with acetate. Cyclic voltammetric results supported the presence of a redox compound(s) associated with the anode biofilm matrix, rather than mobile (dissolved) forms, which could be responsible for the electron transfer to the anode. Scanning electron microscopy revealed that the anode biofilms were comprised of morphologically different cells that were firmly attached on the anode surface and interconnected each other with anchor-like filamentous appendages, which might support the results of cyclic voltammetry. Electronic supplementary material  The online version of this article (doi:) contains supplementary material, which is available to authorized users.