葡萄糖对嗜酸氧化亚铁硫杆菌与Acidiphilium acidophilum共培养的影响

【目的】深入了解自养的嗜酸氧化亚铁硫杆菌(Acidithiobacillus ferrooxidans)与异养的Acidiphilium acidophilum之间的协同作用, 为嗜酸异养微生物在生物浸出体系和酸性矿坑水(AMD)等极端酸性环境中的生态功能研究提供基础, 并为AMD环境的修复提供参考。【方法】应用实时荧光定量PCR (RT-qPCR)及特异性引物, 定量At. ferrooxidans与Aph. acidophilum在类似自然状态下的共培养物受葡萄糖抑制时的生物量变化, 同时检测其生长过程中Fe2+氧化和pH值的变化。【结果】无论是否加入葡萄糖, 共培养对Fe2+氧化的效率均较At. ferrooxidans纯培养高。当葡萄糖浓度为5 g/L时, At. ferrooxidans纯培养失去对Fe2+的氧化能力, 而共培养仍能在100 h内将所有的Fe2+氧化完, 且加入葡萄糖越多的培养体系氧化终点的pH值也越高。在不加入葡萄糖的条件下, At. ferrooxidans 与Aph. acidophilum 数量比在100:1的数量级, 表明以这两种菌为代表的自养菌和异养菌在自然条件下生物量的比例。无论纯培养还是共培养的At. ferrooxidans数量均随葡萄糖浓度的提高而减少, 且延滞期则变长; 而异养生长的Aph. acidophilum则相反。【结论】适合进行Fe2+氧化的At. ferrooxidans与Aph. acidophilum的数量比例范围应在100:1的数量级。由于Aph. acidophilum能促进At. ferrooxidans对亚铁的氧化, 并能缓解或消除葡萄糖对At. ferrooxidans的抑制, 所以不能以加入类似于葡萄糖的有机物作为AMD环境生物修复的手段。     

生物浸出系统中Acidithiobacillus ferrooxidans对雄黄表面改性研究

【目的】研究Acidithiobacillus ferrooxidans BY-3对雄黄表面改性作用,为进一步研究雄黄的生物炮制技术提供实验基础与理论依据。【方法】在4组生物浸出体系中(每组包含100 mL无亚铁离子的9K培养基和0.500 g雄黄):第1组无添加;第2组添加4.469 g硫酸亚铁;第3组添加0.100 g硫粉;第4组加入4.469 g硫酸亚铁和0.100 g硫粉。在上述4组中使用A.ferrooxidans BY-3对雄黄进行生物浸出。浸出前后雄黄表面形貌及元素变化,使用扫描电镜(SEM)与能谱仪(EDS)、X-射线衍射(XRD)、拉曼光谱(Raman)、电感耦合等离子体原子发射光谱仪(ICP-AES)进行分析。【结果】4组浸出体系均发现A.ferrooxidans BY-3粘附于雄黄表面以此来产生直接作用。含Fe2+的浸出体系中雄黄表面产生非常明显的变化,含硫的浸出体系中雄黄表面变化不明显;只有Fe2+存在的浸出体系中As/S比率增高,而其余3组浸出体系中As/S比率均明显下降;另外,改性雄黄的表面存在黄钾铁矾、硫、赤铁矿、针铁矿和磁铁矿等,但未检测到砷华(As2O3)与副雄黄(Pararealgar)。【结论】A.ferrooxidans对雄黄改性具有重要作用。Fe2+对雄黄的改性具有促进作用,而硫对雄黄的改性具有抑制作用。雄黄改性前后的物化分析结果证实了生物浸出技术可有效解决传统方法制备雄黄及贮存过程中氧化和光化问题。     

氧化亚铁硫杆菌铁氧化系统分子生物学研究进展

氧化亚铁硫杆菌（Thiobacillus ferrooxidans,简称T.f）是目前研究最多、最具经济价值的浸矿微生物。由于该菌的能量代谢对于生物浸矿起决定作用,因此其机制的研究必然能促进对该菌生理特性的认识及其遗传改造。氧化亚铁硫杆菌生长方式代表了迄今所知的能够进行生长的热力学极限,可供该菌生长利用的△Eh仅有340mV,氧化Fe2+所能得到的能量很少。在 Fe2+氧化过程中,电子通过电子传递链最终传递给氧,     

嗜酸异养菌对自养菌Acidithiobacillus ferrooxidans金属离子抗性和生物浸出的影响

【目的】了解嗜酸异养菌在诸如酸性矿坑水(AMD)和生物浸出体系等极端酸性环境中对浸矿微生物产生的影响。【方法】研究由嗜酸异养菌Acidiphilium acidophilum和自养菌Acidithiobacillus ferrooxidans经长期驯化后形成的共培养体系分别在Cd2+、Cu2+、Ni2+和Mg2+胁迫下的稳定性;并将此共培养体系应用于黄铁矿和低品位黄铜矿的生物浸出实验。【结果】在上述4种金属离子分别存在的条件下,异养菌Aph.acidophilum均能促进At.ferrooxidans对亚铁的氧化,提高其对能源利用的效率。共培养体系中的异养菌Aph.acidophilum使At.ferrooxidans对Cu2+的最大耐受浓度(MTC)由2.0 g/L提高到5.0 g/L,而且共培养的细胞数量与2.0 g/L Cu2+条件下生长的At.ferrooxidans纯培养相似。另外,共培养中的At.ferrooxidans对Mg2+的MTC也由12.0 g/L提高到17.0 g/L。生物浸出实验中嗜酸异养菌Aph.acidophilum促进了At.ferrooxidans对黄铁矿样品的浸出,浸出率较其纯培养提高了22.7%;但在含铁量较低的低品位黄铜矿浸出体系中共培养和At.ferrooxidans纯培养的浸出率均低于33%。在加入2.0 g/L Fe2+的低品位黄铜矿浸出体系中,共培养和At.ferrooxidans纯培养的浸出率均得到提高,分别达到52.22%和41.27%。【结论】以上结果表明,Aph.acidophilum与At.ferrooxidans共培养在一定的环境胁迫下仍能保持其稳定性并完成各自的生态功能,并且嗜酸异养菌Aph.acidophilum适合在含铁量较高的浸出体系中与铁氧化细菌共同作用来提高生物浸出的效率。     

氧化亚铁硫杆菌亚铁氧化系统的研究进展

氧化亚铁硫杆菌(Acidithiobacillus ferrooxidans)为无机化能自养菌,革兰氏阴性,能在极端酸性环境中生长.由于在生物冶金中的应用及特殊的生理学效应,该菌受到研究者的广泛关注.A.ferrooxidans能氧化亚铁、元素硫及还原态硫化物获得电子,并通过一系列电子载体将电子传递给氧生成水,同时释放能量供生命活动需要.目前对A.ferrooxidans电子传递系统的研究主要集中于亚铁氧化电子传递系统,已发现多种与亚铁氧化电子传递相关电子载体和操纵子,如电子载体铜蓝蛋白(Rustocyanin,Rus)、细胞色素C(Cytochrome C,Cyc)、细胞色素C氧化酶(Cytochrome Coxidase,Cox)、亚铁氧化酶(Iro)、细胞色素bc1复合物(cytochrome bc1 complex,bc1)等,以及rus操纵子和pet操纵子.综述了近年来有关A.ferrooxidans 亚铁氧化电子传递链相关蛋白载体,rus和pet操纵子结构与功能及表达调控等方面的研究进展.     

氧化亚铁硫杆菌固定化技术研究

在生物脱硫过程中 ,以H - 2软性填料作为氧化亚铁硫杆菌 (Thiobacillusferrooxidans)的固定化载体 ,构建了固定床生化反应器。考察了不同稀释率固定下床生化反应器氧化Fe2 + 的情况 ,在通气量为 330L/h ,稀释率为 0 6h-1条件下 ,Fe2 + 最大氧化速率达 7 6 7g[Fe2 + ]/L·h。该反应器连续运行 10 0d,固定化细胞稳定性良好     

漆酶的固定化及其在生物传感器方面的应用

漆酶是一类含铜的多酚氧化酶,它能够催化许多酚类和非酚类物质的氧化.固定化漆酶能改善漆酶的稳定性,实现酶制剂的重复连续使用,具有重要意义.该文综述了漆酶固定化的各种方法,阐述了漆酶相关活性、机械性能和功能等内容,并对漆酶固定化在生物传感器方面的应用作了介绍.     

生物脱硫中氧化亚铁硫杆菌固定化技术的研究

在生物脱硫过程中,以焦碳为填料作为固定化载体,进行了氧化亚硫杆菌的固定化技术研究。在初始pH2、温度为30℃左右、通气量0.5m3/h、喷淋量1.0L/h条件下,挂膜后只需12h,Fe2 氧化率可达95.28%,其Fe2 平均氧化速率是游离细胞时的8倍。氧化亚铁硫杆菌固定化细胞经长期低pH值驯化后,仍能保持对Fe2 具有较高的氧化活性;只需20hFe2 氧化率就达95.05%,Fe2 平均氧化速率达0.38g/(L/h)。     

氧化亚铁硫杆菌分离复壮及固定化的研究

用稀释涂布平板法从已退化的氧化亚铁硫杆菌（Thiobacillus ferrooxidans）菌液中分离出氧化活性较高、生命力强的氧化亚铁硫杆菌T1。以H2软性填料作为氧化亚铁硫杆菌的固定化载体,构建了固定床生物反应器。考察了固定床生物反应器氧化Fe2+的情况：Fe2+最大氧化速率达7.67g/(L·h)。并对固定床生物反应器运行过程中在载体表面形成的沉淀物进行了研究,通过X衍射证明此沉淀物为黄钾铁矾［Kfe3(SO4)2(OH)6］。     

固定化氧化亚铁硫杆菌培养条件对黄铁矾沉淀的影响

以聚乙烯醇-海藻酸钠复合材料为载体,Ca(NO3)2为交联剂对氧化亚铁硫杆菌进行包埋固定化。该固定化细胞的连续培养技术可以用于处理H2S、SO2,为了减少减少固定化细胞培养过程中带来许多不利效应的黄铁矾沉淀 (NH4Fe3(SO4)2(OH)6）,采取了改变初始pH值和目前普遍采用的9K培养基中的(NH4)2SO4浓度,K2HPO4浓度三种方法。结果显示：在三种方法中,降低(NH4)2SO4浓度是比较可行的一种方法,当(NH4)2SO4从3.0 g/L降低到0.5g/L,Fe2+氧化速率几乎没有受到影响,沉淀形成速率却减少了45%。在固定化细胞连续运行时,降低9K培养基中(NH4)2SO4的含量,当稀释率为0.4 h-1,运行时间为96 h,Fe2+氧化速率高达3.75 g/L.H,结果显示反应柱内沉淀明显减少,同时Fe2+氧化速率并没有明显变化。     

Ferrous iron oxidation by foam immobilized Acidithiobacillus ferrooxidans: Experiments and modeling

Ferrous iron bio‐oxidation by Acidithiobacillus ferrooxidans immobilized on polyurethane foam was investigated. Cells were immobilized on foams by placing them in a growth environment and fully bacterially activated polyurethane foams (BAPUFs) were prepared by serial subculturing in batches with partially bacterially activated foam (pBAPUFs). The dependence of foam density on cell immobilization process, the effect of pH and BAPUF loading on ferrous oxidation were studied to choose operating parameters for continuous operations. With an objective to have high cell densities both in foam and the liquid phase, pretreated foams of density 50 kg/m³ as cell support and ferrous oxidation at pH 1.5 to moderate the ferric precipitation were preferred. A novel basket‐type bioreactor for continuous ferrous iron oxidation, which features a multiple effect of stirred tank in combination with recirculation, was designed and operated. The results were compared with that of a free cell and a sheet‐type foam immobilized reactors. A fivefold increase in ferric iron productivity at 33.02 g/h/L of free volume in foam was achieved using basket‐type bioreactor when compared to a free cell continuous system. A mathematical model for ferrous iron oxidation by Acidithiobacillus ferrooxidans cells immobilized on polyurethane foam was developed with cell growth in foam accounted by an effectiveness factor. The basic parameters of simulation were estimated using the experimental data on free cell growth as well as from cell attachment to foam under nongrowing conditions. The model predicted the phase of both oxidation of ferrous in shake flasks by pBAPUFs as well as by fully activated BAPUFs for different cell loadings in foam. Model for stirred tank basket bioreactor predicted within 5% both transient and steady state of the experiments closely for the simulated dilution rates. Bio‐oxidation at high Fe²⁺ concentrations were simulated with experiments when substrate and product inhibition coefficients were factored into cell growth kinetics. © 2009 American Institute of Chemical Engineers Biotechnol. Prog., 2009     

High-rate ferrous iron oxidation by immobilized Acidithiobacillus ferrooxidans with complex of PVA and sodium alginate

By four different methods, Acidithiobacillus ferrooxidans cells were immobilized by the complex of PVA and sodium alginate. The beads formed by these different methods were evaluated in terms of relative mechanical strength, biological activity, dilatability, and so on. The results indicate that the technique utilizing the complex of PVA and sodium alginate crosslinked with Ca(NO(3))(2) is more appropriate for the immobilization of A. ferrooxidans than any others. So the PVA-calcium nitrate beads were used in batch and continuous culture. A maximum ferrous iron oxidation rate of 4.6 g/l/h was achieved in batch culture. Long-time performance of packed-bed bioreactor was evaluated systematically over 40 days, depending on the conversion ratio of ferrous iron and the residence time. At a residence time of 2.5 h, 96% of the initial ferrous iron was oxidized. This study shows this new immobilization technique will be a feasible and economical method for A. ferrooxidans.     

Effect of ferrous iron concentration on the catalytic activity of immobilized cells of Thiobacillus ferrooxidans

 The kinetics of continuous oxidation of ferrous iron by immobilized cells of Thiobacillus ferrooxidans was studied in a packed-bed bioreactor. Polyurethane foam biomass support particles were used as carriers for cell immobilization. Effects of ferrous iron concentration and its volumetric loading on the kinetics of the reaction were investigated. Media containing different concentrations of ferrous iron in the range 5–20 kg m^-3 were tested. For each medium the kinetics of the reaction at different volumetric loadings of ferrous iron, at a constant temperature of 30^°C, were determined. With media containing 5 kg m^-3 and 10 kg m^-3 Fe²⁺, the fastest oxidation rates of 34.25 kg m^-3 h^-1 and 32 kg m^-3 h^-1 were achieved at a dilution rate of around 6 h^-1, which represents a residence time of 10 min. Employing a higher concentration of ferrous iron (20 kg m^-3) in the medium resulted in lower oxidation rates, with a maximum value of 10 kg m^-3 h^-1, indicating an inhibitory effect of ferrous iron on growth and activity of T. ferrooxidans. The reliable performance of the bioreactor during the course of the experiments confirmed the suitability of polyurethane foam biomass support particles as carriers for T. ferrooxidans immobilization. Received: 5 December 1995/Received revision: 21 April 1996/Accepted: 29 April 1996     

Development of an optimal medium for continuous ferrous iron oxidation by immobilized Acidothiobacillus ferrooxidans cells

This study was aimed at developing an immobilized bioreactor system in which long-term continuous ferrous iron oxidation can be realized with no formation of jarosite, which causes clogging of support pores and reactor lines. For this purpose, a medium with no jarosite formation was developed first by selecting optimal nitrogen and phosphate sources and their concentrations. Then with the developed medium containing ammonium phosphate instead of ammonium sulfate and potassium phosphate, repeated batch and continuous operations of ferrous iron oxidation by Acidothiobacillus ferrooxidans cells immobilized in a depth filter were successfully performed for an extended period of time. For about 510 h of operation including 450 h of continuous operation at dilution rates of 0.1, 0.2, and 0.3 h(-)(1), no formation of jarosite and thus no clogging of the reactor system were observed. The maximum ferrous iron oxidation rate was as high as 2.6 g/(L.h) at a dilution rate of 0.3 h(-)(1).     

Immobilization of Acidithiobacillus ferrooxidans by a PVA–boric acid method for ferrous sulphate oxidation

Acidithiobacillus ferrooxidans was immobilized in poly(vinyl alcohol) (PVA) by a PVA–boric acid method, and spherical beads of uniform size were produced. Biooxidation of ferrous iron by immobilized cells was investigated in repeated batch culture and continuous operation in a laboratory scale packed-bed bioreactor. During repeated batch culture, the cell-immobilized gels were stable and showed high constant iron-oxidizing activity. In continuous operation in a packed-bed bioreactor, biooxidation of ferrous iron fits a plug-flow reaction model well. A maximum Fe²⁺ oxidation rate of 1.89 g l⁻¹ h⁻¹ was achieved at the dilution rate of 0.38 h⁻¹ or higher, while no obvious precipitate was detected in the bioreactor.     

Biological ferrous sulfate oxidation by A. ferrooxidans immobilized on chitosan beads

The immobilization of Acidithiobacillus ferrooxidans cells on chitosan and cross-linked chitosan beads and the biooxidation of ferrous iron to ferric iron in a packed-bed bioreactor were studied. The biofilm formation was carried out by using a glass column reactor loaded with chitosan or cross-linked chitosan beads and 9 K medium previously inoculated with A. ferrooxidans cells. The immobilization cycles on the carrier matrix with the bioreactor operating in batch mode were compared. Then, the reactor was operated using a continuous flow of 9 K medium at different dilution rates. The results indicate that the packed-bed reactor allowed increasing the flow rate of medium approximately two fold (chitosan) and eight fold (chitosan cross-linked) without cells washout, compared to a free cell suspension reactor used as control, and to reach ferric iron productivities as high as 1100 and 1500 mg l(-1) h(-1) respectively. Scanning electron microscopy micrographs of the beads, infrared spectroscopy and the X-ray diffraction patterns of precipitates on the chitosan beads were also investigated.     

High-rate acidophilic ferrous iron oxidation in a biofilm airlift reactor and the role of the carrier material

In this study, the feasibility and engineering aspects of acidophilic ferrous iron oxidation in a continuous biofilm airlift reactor inoculated with a mixed culture of Acidithiobacillus ferrooxidans and Leptospirillum ferrooxidans bacteria were investigated. Specific attention was paid to biofilm formation, competition between both types of bacteria, ferrous iron oxidation rate, and gas liquid mass transfer limitations. The reactor was operated at a constant temperature of 30 degrees C and at pH values of 0-1.8. Startup of the reactor was performed with basalt carrier material. During the experiments the basalt was slowly removed and the ferric iron precipitates formed served as a biofilm carrier. These precipitates have highly suitable characteristics as a carrier material for the immobilization of ferrous iron-oxidizing bacteria and dense conglomerates were observed. Lowering the pH (0.6-1) resulted in dissolution of the ferric precipitates and induced granular sludge formation. The maximum ferrous iron oxidation rate achieved in this study was about 145 molFe(2+)/m(3).h at a hydraulic residence time of 0.25 h. Optimal treatment performance was obtained at a loading rate of 100 mol/m(3).h at a conversion efficiency as high as 98%. Fluorescent in situ hybridization (FISH) studies showed that when the reactor was operated at high ferrous iron conversion (>85%) for 1 month, the desirable L. ferrooxidans species could out-compete A. ferrooxidans due to the low Fe(2+) and high Fe(3+) concentrations.     

Comparison of ferric iron generation by different species of acidophilic bacteria immobilized in packed-bed reactors

Flooded packed-bed bioreactors, prepared by immobilizing four different species of acidophilic iron-oxidizing bacteria on porous glass beads, were compared for their ferric iron-generating capacities when operated in batch and continuous flow modes over a period of up to 9 months, using a ferrous iron-rich synthetic liquor and acid mine drainage (AMD) water. The bacteria used were strains of Acidithiobacillus ferrooxidans, Leptospirillum ferrooxidans, a Ferrimicrobium-like isolate (TSTR) and a novel Betaproteobacterium (isolate PSTR), which were all isolated from relatively low-temperature mine waters. Three of the bacteria used were chemoautotrophs, while the Ferrimicrobium isolate was an obligate heterotroph. Greater biomass yields achievable with the Ferrimicrobium isolate resulted in greater iron oxidation efficiency in the newly commissioned bioreactor containing this bacterium, though long-term batch testing with organic carbon-free solution resulted in similar maximum iron oxidation rates in all four bioreactors. Two of the bioreactors (those containing immobilized L. ferrooxidans and Ferrimicrobium TSTR) were able to generate significantly lower concentrations of ferrous iron than the others when operated in batch mode. In contrast, when operated as continuous flow systems, the bioreactor containing immobilized PSTR was superior to the other three when challenged with either synthetic or actual AMD at high flow rates. The least effective bacterium overall was At. ferrooxidans, which has previously been the only iron-oxidizer used in the majority of reports describing ferric iron-generating bioreactors. The results of these experiments showed that different species of iron-oxidizing acidophiles have varying capacities to oxidize ferrous iron when immobilized in packed-bed bioreactors, and that novel isolates may be superior to well-known species.     

Mathematical model of the oxidation of ferrous iron by a biofilm of Thiobacillus ferrooxidans

Microbial oxidation of ferrous iron may be a viable alternative method of producing ferric sulfate, which is a reagent used for removal of H(2)S from biogas. The paper introduces a kinetic study of the biological oxidation of ferrous iron by Thiobacillus ferrooxidans immobilized on biomass support particles (BSP) composed of polyurethane foam. On the basis of the data obtained, a mathematical model for the bioreactor was subsequently developed. In the model described here, the microorganisms adhere by reversible physical adsorption to the ferric precipitates that are formed on the BSP. The model can also be considered as an expression for the erosion of microorganisms immobilized due to the agitation of the medium by aeration.     

Dynamic relaxometry: application to iron uptake by ferritin

We introduce dynamic relaxometry as a novel technique for studying biochemical reactions, such as those leading to mineral formation (biomineralization). This technique was applied to follow the time course of iron oxidation and hydrolysis by the protein ferritin. Horse spleen apoferritin was loaded with single additions of 4, 10, 20, 40, and 100 ferrous ions per protein, and with multiple additions of 4, 10, 20, and 100 ferrous ions. The NMR T2 relaxation time was then measured sequentially and continuously for up to 24 h. At low loading factors of 4-10 Fe atoms/molecule, the iron is rapidly bound and oxidized by the protein on a time scale of approximately 15 s to several minutes. At intermediate loading factors (10-40), rapid initial oxidation was observed, followed by the formation of antiferromagnetic clusters. This process occurred at a much slower rate and continued for up to several hours, but was inhibited at lower pH values. At higher loading factors (40-1000), iron oxidation may occur directly on the core, and this process may continue for up to 24 h following the initial loading. Dynamic relaxometry appears to be a potentially powerful technique that may well have applications beyond the study of iron uptake by the ferritin protein.