响应面法优化Fe~(2+)的微生物氧化条件

氧化亚铁钩端螺旋菌(Leptospirillum ferrooxidans,L.f)是一种极端嗜酸,专性自养氧化铁的细菌,能够耐受较低pH和较高的温度,被广泛应用于生物浸矿和环境治理。氧化亚铁钩端螺旋体菌的生物浸矿效率与其对Fe~(2+)氧化速率相关,因此,本文采用响应面法,通过建立二次多项式回归方程考察pH、温度、Fe~(2+)浓度及转速四个培养因素对Fe~(2+)氧化速率的影响。结果显示在pH为2.25、温度为32℃、初始Fe~(2+)浓度为175.36 mmol/L、转数为165 r/min时,Fe~(2+)最高氧化速率为0.2911 g/Lh。     

Analysis of muramic acid in holocene microbial environments by gas chromatography,electron impact,and fast atom bombardment mass spectrometry

Analytical procedures have been modified to determine the abundance of muramic acid in four different Holocene sediment samples. Muramic acid is specific to the peptidoglycan moiety of the cell walls of most eubacterial pro‐karyotic organisms. The following procedure seemed to be the most appropriate for the detection of muramic acid and amino acids, including diaminopimelic acid. Hydrolysis of the samples (in 6 N HCl, 4.5 h, at 100°C) was followed by separation and purification of amino sugars and amino acids using Amberlite XAD‐2 and then Bio‐Rad AG 50W‐X8 resins. The N,O‐heptafluorobutyryl‐n‐butyl ester derivatives were prepared by esterification in acidified (3 N HCl) n‐butanol for 3 h at 100°C, followed by acylation by refluxing with heptafluorobutyric anhydride in acetonitrile (2:1 v/v) for 12 min at 150°C. The derivatives were analyzed by gas chromatography (GC) and gas chromatography‐mass spectrometry. Fast atom bombardment (FAB) ionization was used for the muramic acid derivative to determine its molecular weight and structure, d‐and l‐amino acids were separated by GC and a capillary chiral column. By using this technique a stable N,O‐heptafluo‐robutyryl‐n‐butyl ester derivative of muramic acid was identified at picogram levels in Holocene sedimentary microbial communities. It has been reported previously that microorganisms in sediments rapidly degrade muramic acid from cell walls of dead prokaryotes. Kinetic experiments revealed that muramic acid was relatively stable in intact cell walls but decomposed rapidly in the free form. These investigations noted above showed that the concentration of muramic acid may be used as an indicator of the presence of the intact cell walls of cyanobacteria and most other bacteria in Holocene microbial communities, and of microbial contamination in samples older than the Holocene.     

Identification of Flavone Compounds in Eighteen Gramineae Species

Conditions for tryptophan synthesis from pyruvic acid, indole and NH₄Cl by Enterobacter aerogenes AHU 1540 having a high tryptophanase activity, were investigated using a reaction mixture containing 1.7% of pyruvic acid. Under optimum conditions, 16.4g/liter of tryptophan was accumulated after 24 hr of incubation.

Agaricus campestris AHU 9382 produced pyruvic acid in amounts of 22 ~ 26.5 g/liter from 5% of glucose after 3-days shaking culture. When E. aerogenes was added to this fermentation broth together with indole and NH₄Cl, pyruvic acid produced was rapidly converted to tryptophan and yields of tryptophan as high as 15 g/liter were obtained after 12 hr of incubation. Furthermore, pyruvic acid fermentation by Saccharomyces exiguus AHU 3110 or Corynebacterium sp. 37-3A could also be used as a pyruvic acid source for subsequent tryptophan production.     

Activation of bovine plasminogen by Streptococcus uberis

Abstract Thiosulfate and tetrathionate oxidation activity of Thiobacillus ferrooxidans were found to be absent in iron-growth cell as well as in the cells grown anaerobically on elemental sulfur. While the thiosulfate oxidase activity was absent in the cell-free extract of the above cells, the activity of rhodanese was present irrespective of the culture condition of T. ferrooxidans . It is thus conceivable that rhodanese is not involved in thiosulfate metabolism. During growth in presence of ferrous sulfate plus elemental sulfur, the thiosulfate/tetrathionate oxidation activity was absent till the oxidation of ferrous iron was complete and the cells harvested only in the latter period acquired the thiosulfate/tetrathionate oxidation activity. Thus it becomes evident that the inhibition of thiosulfate and tetrathionate oxidation is solely due to presence of ferrous iron.     

Stoichiometric model and flux balance analysis for a mixed culture of Leptospirillum ferriphilum and Ferroplasma acidiphilum

The oxidation process of sulfide minerals in natural environments is achieved by microbial communities from the Archaea and Bacteria domains. A metabolic reconstruction of two dominant species, Leptospirillum ferriphilum and Ferroplasma acidiphilum, which are always found together as a mixed culture in this natural environments, was made. The metabolic model, composed of 152 internal reactions and 29 transport reactions, describes the main interactions between these species, assuming that both use ferrous iron as energy source, and F. acidiphilum takes advantage of the organic compounds secreted by L. ferriphilum for chemomixotrophic growth. A first metabolic model for a mixed culture used in bacterial leaching is proposed in this article, which pretends to represent the characteristics of the mixed culture in a simplified manner. It was evaluated with experimental data through flux balance analysis (FBA) using as objective function the maximization of biomass. The growth yields on ferrous iron obtained for each microorganism are consistent with experimental data, and the flux distribution obtained allows understanding of the metabolic capabilities of both microorganisms growing together in a bioleaching process. The model was used to simulate the growth of F. acidiphilum on different substrates, to determine in silico which compounds maximize cell growth, and which are essential. Knockout simulations were carried out for L. ferriphilum and F. acidiphilum metabolic models, predicting key enzymes of central metabolism. The results of this analysis are consistent with experimental data from literature, showing a robust behavior of the metabolic model. © 2014 American Institute of Chemical Engineers Biotechnol. Prog., 31:307–315, 2015     

Inhibition effect of ferric iron on the kinetics of ferrous iron

Ferric iron acted as a non-competitive inhibitor for the biological oxidation of ferrous iron and decreased the inhibitory effects of high concentrations of ferrous iron as well as the auto-inhibitive effect the bacterial cells. A previously developed kinetic model for this reaction was modified to incorporate the inhibition effects of ferric iron. © Rapid Science Ltd. 1998     

Isolation and Characterization of Acidithiobacillus ferrooxidans Strain D3-2 Active in Copper Bioleaching from a Copper Mine in Chile

Acidithiobacillus ferrooxidans strain D3-2, which has a high copper bioleaching activity, was isolated from a low-grade sulfide ore dump in Chile. The amounts of Cu²⁺ solubilized from 1% chalcopyrite (CuFeS₂) concentrate medium (pH 2.5) by A. ferrooxidans strains D3-2, D3-6, and ATCC 23270 and 33020 were 1360, 1080, 650, and 600 mg·l ^?1·30 d^?1. The iron oxidase activities of D3-2, D3-6, and ATCC 23270 were 11.7, 13.2, and 27.9 μl O₂ uptake·mg protein^?1·min^?1. In contrast, the sulfite oxidase activities of strains D3-2, D3-6, and ATCC 23270 were 5.8, 2.9, and 1.0 μl O₂ uptake·mg protein^?1·min^?1. Both of cell growth and Cu-bioleaching activity of strains D3-6 and ATCC 23270, but not, of D3-2, in the chalcopyrite concentrate medium were completely inhibited in the presence of 5 mM sodium bisulfite. The sulfite oxidase of strain D3-2 was much more resistant to sulfite ion than that of strain ATCC 23270. Since sulfite ion is a highly toxic intermediate produced during sulfur oxidation that strongly inhibits iron oxidase activity, these results confirm that strain D3-2, with a unique sulfite resistant-sulfite oxidase, was able to solubilize more copper from chalcopyrite than strain ATCC 23270, with a sulfite-sensitive sulfite oxidase.     

Effects of the oxygen transfer rate on ferrous iron oxidation by Thiobacillus ferrooxidans

Ferrous iron oxidation by Thiobacillus ferrooxidans was studied in shake flasks and a bubble column under different aeration conditions. The maximum biooxidation rate constant was affected by oxygen transfer only at low aeration intensities. At oxygen transfer rates higher than 0.03 mmol O₂ l⁻¹ min⁻¹, the maximum biooxidation rate constant was about 0.050 h⁻¹ in both shake flasks of different size and the bubble column. The oxygen transfer rate could be used as a basis for scaling up bioreactors for ferrous iron biooxidation by T. ferrooxidans.     

Cumulative Title Index

Abstract

Quantitative data on the speciation of chitosan (310 kDa) with low and high molecular weight carboxylates in aqueous solution are reported. The following carboxylic ligands were considered: monocarboxylate (butyrate); dicarboxylates (malonate, succinate, azelate); tricarboxylate (1,2,3-propa-netricarboxylate); tetracarboxylate (1,2,3,4-butanetetracarboxylate); polyacrylates (2.0 and 20 kDa); polymethacrylate (5.4 kDa). The investigation was performed by potentiometry at t =25°C, at low ionic strength (without addition of supporting electrolyte) and at I =0.15mol L^?1 (NaCl). For all the systems the formation of (chitosan)LH_i species was found (L = carboxylic ligand; i = 1 to 4 depending on the carboxylic ligand considered). The stability of proton–chitosan–carboxylate species depends on the number of carboxylic groups involved in the complexation, and it was possible to calculate a rough free energy value per bond ΔG_n = ?15±2kJ mol^?1. By using the stability data, the quantitative sequestering capacity of chitosan towards the carboxylates here considered [expressed as the-log(total chitosan concentration) necessary to bind 50% of carboxylate, i.e., pL₅₀] was calculated for different pH values, at low ionic strength and at I =0.15 mol L^?1. The pL₅₀ values, ranging from 3 to 7, show that chitosan is quite a strong sequestering agent towards carboxylates. Evidences were also obtained for the different behaviour between low and high molecular weight carboxylates.     

Forms of iron in the oxygenated waters of Esthwaite Water,U.K.

Flow centrifugation at an acceleration of 18 000 × gravity of surface water samples of Esthwaite Water separates the iron into two fractions, the sediment (A) and the supernatant (B). The amounts of iron in A and B are approximately equal (40–60%) except during, and for a few months after, the annual overturn. At this time there is a large increase in the total iron concentration, the extra iron being found in fraction A. Electron microscopic examination and microprobe analysis of fraction A collected at times other than the overturn period show that the most prevalent form of iron in this fraction is amorphous iron (III) oxide. The oxide consists of approximately spherical, ellipsoidal or cylindrical particles, hardly any of which have a dimension >0.5 μm. In the lake, sedimentation of iron probably requires the particles to flocculate either by self-association or by association with other particulate matter. The particles contain highly variable amounts of Ca, also Si, P and S, and probably humic substances. Kinetic analyses of Fe (III) species, carried out by measuring rates of formation of Fe³⁺ on treatment with acid, show that fraction A contains a single slow-reacting species which can be equated with the amorphous iron oxide. Fraction B contains this species also, together with a component which reacts about 30 times faster, and which comprised approximately 15% of the iron in an unconcentrated surface water sample. The nature of the fast-reacting component is not clear. Possibly it consists of small unaged oxide polymers; alternatively it might be composed of iron-organic complexes.     

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